WO2004052602A2 - Hydrophobing process and apparatus - Google Patents
Hydrophobing process and apparatus Download PDFInfo
- Publication number
- WO2004052602A2 WO2004052602A2 PCT/GB2003/005202 GB0305202W WO2004052602A2 WO 2004052602 A2 WO2004052602 A2 WO 2004052602A2 GB 0305202 W GB0305202 W GB 0305202W WO 2004052602 A2 WO2004052602 A2 WO 2004052602A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- emulsion
- hydrophobing
- homogeniser
- miniplant
- mother plant
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B27—WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
- B27N—MANUFACTURE BY DRY PROCESSES OF ARTICLES, WITH OR WITHOUT ORGANIC BINDING AGENTS, MADE FROM PARTICLES OR FIBRES CONSISTING OF WOOD OR OTHER LIGNOCELLULOSIC OR LIKE ORGANIC MATERIAL
- B27N1/00—Pretreatment of moulding material
- B27N1/006—Pretreatment of moulding material for increasing resistance to swelling by humidity
Definitions
- the present invention relates in general to hydrophobing and in particular to a process for hydrophobing fibrous and particulate material in the manufacture of reconstituted wood products (RWP).
- RWP reconstituted wood products
- the fibrous and/or particulate wood matter (called furnish) are impregnated with emulsions and resin glue.
- the emulsions may be used pre-blended with the glue, or the two components may be used separately.
- Heat and pressure are used to cure the resin glue and drive off water to form the RWP.
- the RWP may be in the form of boards which can be used as construction material.
- each miniplant comprising an homogeniser for producing a hydrophobing emulsion from water, surfactant composition and said wax and being operably connected, optionally with intermediate storage, for supplying hydrophobing emulsion to one or more impregnators for impregnating fibrous and/or particulate material with hydrophobing emulsion in the manufacture of reconstituted wood products'
- introducing water, surfactant composition and said wax to each miniplant homogeniser to produce a hydrophobing emulsion supplying hydrophobing emulsion to said impregnators from said mother plant and from said one or more miniplant homogenisers; and (vi) impregnating fibrous and/or particulate material with hydrophobing emulsion in each impregnator to produce reconstituted wood products.
- apparatus for hydrophobing fibrous and/or particulate material in the manufacture of reconstituted wood products which comprises :
- a mother plant comprising a first homogeniser for generating a hydrophobing emulsion from wax, surfactant composition and water; and (b) one or more miniplants at one or more locations remote from said mother plant, each miniplant comprising an homogeniser for generating a hydrophobing emulsion from water, surfactant composition and said wax and being connected, optionally with intermediate storage, to one or more impregnators for impregnating fibrous and/or particulate material with hydrophobing emulsion in the manufacture of reconstituted wood products.
- the present invention solves the technical problem identified above by providing each impregnator with alternative sources of supply of hydrophobing emulsion.
- one source of supply of hydrophobing emulsion is the mother plant homogeniser and another source of supply is the one or more miniplant homogenisers.
- a further advantage of the present invention is that at least part of the services required for the miniplant homogeniser may be integrated with those associated with the impregnator. This could result in cost savings and the like.
- Such integrated services may comprise water, steam, storage tanks, electricity, water softening and sites buildings.
- existing storage facilities at the customer site which were previously used to store the high stock levels of emulsion needed when supplied from a remote manufacturing facility, could be utilised for the raw material and finished product storage from the one or more mini plants.
- sites which have resin- manufacturing facilities will have excess steam and softened water as part of said resin manufacture. These materials can be utilised advantageously as services for the one or more miniplants.
- each miniplant has a production capacity which is less than that of the mother plant homogeniser.
- the impregnators may be supplied simultaneously with emulsion from the mother plant and from one or more miniplants.
- the impregnators may be supplied with emulsion alternatively from the mother plant and the one or more miniplants.
- the majority (>50%) and more preferably between 90 % and 95 % of the emulsion supplied to the one or more impregnators is supplied from the one or more miniplants.
- the hydrophobing emulsion is predominantly (> 50%) supplied to the one or more impregnators from the one or more miniplant homogenisers. Hydrophobing emulsion is then supplied from the mother plant intermittently, when the miniplant homogeniser(s) is/are not available, for example because of maintenance or other shutdown reasons.
- This has an advantage that the transportation cost of the emulsion can be reduced because the emulsion need not be predominantly transported from the mother plant. However, continuity of supply is assured by the presence of the mother plant.
- the surfactant composition used to produce the emulsions in the mother plant homogeniser may be different to the surfactant composition used to produce the emulsions in the one or more miniplant homogenisers.
- the concentration of surfactant composition in the emulsions produced by each of the one or more miniplants homogenisers may be different to the concentration of surfactant composition in the emulsion produced by the mother plant homogeniser.
- the emulsions produced by the one or more miniplant homogenisers have a lower concentration of surfactant composition than in the emulsion produced by the mother plant homogeniser.
- the concentration of water in the emulsions produced by each of the one or more miniplant homogenisers may be different to the concentration of water in the emulsion produced by the mother plant homogeniser.
- the emulsions produced by the one or more miniplant homogenisers have a larger concentration of water than in the emulsion produced by the mother plant homogeniser.
- the hydrophobing emulsion produced by each of the one or more miniplant homogenisers is more dilute than the hydrophobing emulsion produced by the mother plant. If a high shear type homogeniser is used there is a further advantage that the emulsion particle sizes and more dilute emulsion means that a lower concentration of surfactant composition can be used with the miniplant homogeniser emulsions, with associated lower cost.
- a hydrophobing emulsion produced by the one or more miniplants may comprise a wax in a concentration in the range 30 to 70 % by weight and a surfactant composition in a concentration of less than 5 % by weight, preferably less than 3 % by weight, the balance consisting essentially of water.
- Suitable waxes are Slackwax.
- the surfactant compositions used in the present invention may be selected from the group consisting of non-ionic surfactant compositions, anionic surfactant compositions, cationic surfactant compositions and mixtures thereof.
- Anionic and nonionic surfactant compositions may comprise one or more fatty acids and/or esters thereof, or one or more ammonium compounds.
- Suitable fatty acids include C14 and C16 fatty acids, oleic acid, stearic acid and tallows.
- Suitable ammonium compounds include ammonia, monoethanolamine (MEA), diethanolamine (DEA), triethanolamine (TEA), morpholine and dimethyl amin ⁇ ethanol (DMAE).
- the surfactant compositions may comprise compounds other than stearic acid which have stearyl functional groups such as glycerol monostearate (GMS) and stearyl alcohols, for example, acetostearyl alcohol.
- the surfactant compositions used in the present invention may comprise one or more additives selected from the group consisting of stabilisers, neutralisers and biocides.
- the hydrophobing emulsions used in the present invention may comprise one or more additives selected from the group consisting of stabilisers, neutralisers and biocides.
- the low surfactant emulsions of the present invention are not normally producible using conventional homogenisation technology. Advantages of using an emulsion with a lower concentration of surfactant composition include reduced cost and an improved hydrophobing capability.
- the miniplant homogenisers are of the high sheer mixer type such as a Supraton ® manufactured by BWS, rather than the high pressure type.
- the homogeniser is skid-mounted so that it may be moved and located at impregnation plants wherever required.
- Particularly preferred emulsion compositions by weight are :
- Figure 1 illustrates in schematic form a mother plant according to the present invention.
- Figure 2 represents in schematic form a miniplant according to the present invention.
- Figure 1 illustrates in schematic form a mother plant according to the present invention.
- the mother plant comprises a storage tank (1) for wax phase and a storage tank (2) for a water phase including surfactant composition.
- the tanks (1) (2) are operably connected to a blend tank or metered blend pump (3) and thence to a homogeniser (4).
- water phase (including surfactant composition) and wax phase from the storage tanks (1) (2) are passed through the blend tank or metered blend pump (3) and introduced into the homogeniser (4) which produces a mother plant emulsion.
- FIG. 2 represents in schematic form a miniplant according to the present invention.
- the miniplant is located remotely from a mother plant such as shown in Figure 1.
- the miniplant comprises a storage tank for wax (21) and a storage 1 tank (22) for water phase including surfactant composition.
- the tanks (21)(22) are operably connected to a blend tank or metered blend pump (23) and thence to a homogeniser (24) such as a high sheer mixer type homogeniser e.g. a Supraton ® manufactured by BWS
- the homogeniser (24) is operably connected to an intermediate storage tank (25).
- the intermediate storage tank (25) and the homogeniser (24) are operably connected to an impregnator (30).
- wax phase from tank (21) and water phase (including surfactant composition) from tank (22) are passed through blend tank or metered blend pump (24) and introduced into the homogeniser (24) which produces a hydrophobing emulsion.
- the emulsion is supplied directly to the impregnator (30).
- the emulsion maybe supplied indirectly to the impregnator through storage tank (25).
- fibrous and/or particulate material is hydrophobed with the emulsion to produce reconstituted wood products.
- the emulsion supplied to the impregnator may be predominantly supplied by the miniplant homogeniser. However, when emulsion from the miniplant is not available then emulsion may be provided from the remote mother plant such as shown in Figure 1 by road tanker or other transport means through dispatch loading facility (6).
- miniplant may be integrated with services such as electricity,, softened water etc at the impregnator site.
- the emulsion used for hydrophobing which is supplied by the miniplants may have a lower surfactant composition concentration than the emulsion produced by the mother plant, which reduces costs for example.
- a 20 tonne batch of emulsion was produced by a high sheer mixer type Supraton" homogeniser manufactured by BWS. The emulsion was successfully used to hydrophobe fibrous and/or particulate material over a three day period. Thereafter emulsion was supplied from a motherplant.
- compositions of the mother plant and miniplant emulsions are shown in the Table.
- the wax used was a hydrocarbon wax and the surfactant composition was an anionic surfactant composition comprising stearic compounds and monoethanolamine.
Abstract
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP03778558A EP1572426A2 (en) | 2002-12-11 | 2003-12-03 | Hydrophobing process and apparatus |
AU2003285560A AU2003285560A1 (en) | 2002-12-11 | 2003-12-03 | Hydrophobing process and apparatus |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB0228912A GB0228912D0 (en) | 2002-12-11 | 2002-12-11 | Process and apparatus |
GB0228912.2 | 2002-12-11 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2004052602A2 true WO2004052602A2 (en) | 2004-06-24 |
WO2004052602A3 WO2004052602A3 (en) | 2004-08-12 |
Family
ID=9949512
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/GB2003/005202 WO2004052602A2 (en) | 2002-12-11 | 2003-12-03 | Hydrophobing process and apparatus |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP1572426A2 (en) |
AU (1) | AU2003285560A1 (en) |
GB (1) | GB0228912D0 (en) |
WO (1) | WO2004052602A2 (en) |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB519618A (en) * | 1938-06-20 | 1940-04-02 | Thurstan Wyatt Dickeson | Improvements in and relating to, aqueous emulsions of wax and allied materials and to products and articles containing, impregnated, coated, or surface-sized with the same or resulting from treatment with the same |
US4993839A (en) * | 1989-03-20 | 1991-02-19 | Astec Industries, Inc. | Method and apparatus for producing asphaltic mix |
DE4035050A1 (en) * | 1990-11-05 | 1992-05-07 | Benninghoven Gmbh & Co Kg | Asphalt mixing process - involves preparing heated and weighed granule charges to be held at satellite plant for mixing with molten asphalt |
US6274199B1 (en) * | 1999-01-19 | 2001-08-14 | Chemical Specialties, Inc. | Wood treatment process |
WO2001076837A1 (en) * | 2000-04-07 | 2001-10-18 | Exxonmobil Oil Corporation | Timber preservative |
-
2002
- 2002-12-11 GB GB0228912A patent/GB0228912D0/en not_active Ceased
-
2003
- 2003-12-03 EP EP03778558A patent/EP1572426A2/en not_active Withdrawn
- 2003-12-03 WO PCT/GB2003/005202 patent/WO2004052602A2/en not_active Application Discontinuation
- 2003-12-03 AU AU2003285560A patent/AU2003285560A1/en not_active Abandoned
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB519618A (en) * | 1938-06-20 | 1940-04-02 | Thurstan Wyatt Dickeson | Improvements in and relating to, aqueous emulsions of wax and allied materials and to products and articles containing, impregnated, coated, or surface-sized with the same or resulting from treatment with the same |
US4993839A (en) * | 1989-03-20 | 1991-02-19 | Astec Industries, Inc. | Method and apparatus for producing asphaltic mix |
DE4035050A1 (en) * | 1990-11-05 | 1992-05-07 | Benninghoven Gmbh & Co Kg | Asphalt mixing process - involves preparing heated and weighed granule charges to be held at satellite plant for mixing with molten asphalt |
US6274199B1 (en) * | 1999-01-19 | 2001-08-14 | Chemical Specialties, Inc. | Wood treatment process |
WO2001076837A1 (en) * | 2000-04-07 | 2001-10-18 | Exxonmobil Oil Corporation | Timber preservative |
Also Published As
Publication number | Publication date |
---|---|
AU2003285560A1 (en) | 2004-06-30 |
WO2004052602A3 (en) | 2004-08-12 |
EP1572426A2 (en) | 2005-09-14 |
GB0228912D0 (en) | 2003-01-15 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN100558520C (en) | The bamboo fiberboard preparation method of modified soy protein adhesive | |
CN101791817B (en) | Production method of environmental-friendly type low-cost middle and high density fiber board | |
EP1058607B1 (en) | Wood composite products | |
US8652633B2 (en) | Nanoparticulate wax dispersions, process for preparing them and method of hydrophobicizing materials using them | |
CN105026512A (en) | Compositions that include hydrophobizing agents and stabilizers and methods for making and using same | |
EP1112983A2 (en) | Application of a diisocyanate for producing composite gypsum board | |
CN102561113A (en) | Wood fiber board and manufacturing method thereof | |
CN101597482A (en) | A kind of emulsion paraffin water repellent for fiber board | |
WO2004052602A2 (en) | Hydrophobing process and apparatus | |
CN102877359A (en) | Composite curing agent and application of composite curing agent to production of melamine impregnated paper | |
US20090095431A1 (en) | Paper-Sizing Emulsion, Process for Preparing It and Use Thereof | |
CN103304822A (en) | Production technology for emulsifying rosin resin | |
Banik | Manufacturing of bamboo composite in the industrial aspect | |
CN105968382B (en) | A kind of more amine cations of lignin split type asphalt emulsifier and preparation method thereof soon | |
CN101565603A (en) | Waterproof agent for fibreboard | |
CN102127286B (en) | New water-soluble epoxy emulsion and preparation method thereof | |
CN100445466C (en) | Weak acid rosin emulsion gluing agent and its common technology | |
CN1417410A (en) | Neutral rosin sizing agent and its prepn | |
CN109837110A (en) | Heatproof diesel oil emulsifier | |
WO2001032780A1 (en) | Wax compound | |
CN101076568B (en) | Method for the production of a modified montan wax, a modified montan wax and use of modified montan wax for production of an aqueous montan wax composition | |
CN102337706A (en) | White card packing paper antifoaming agent as well as preparation method and application thereof | |
CN107406567B (en) | Binder composition and use thereof in a method for producing wood fibre boards | |
DE102021122602B4 (en) | Plant and process for the continuous production of ammonia using renewable energies | |
CN108424511B (en) | Method for preparing water-based polyester resin by using printing and dyeing slurry residues and application |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A2 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SY TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW |
|
AL | Designated countries for regional patents |
Kind code of ref document: A2 Designated state(s): BW GH GM KE LS MW MZ SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IT LU MC NL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
WWE | Wipo information: entry into national phase |
Ref document number: 2003778558 Country of ref document: EP |
|
WWP | Wipo information: published in national office |
Ref document number: 2003778558 Country of ref document: EP |
|
WWW | Wipo information: withdrawn in national office |
Ref document number: 2003778558 Country of ref document: EP |
|
NENP | Non-entry into the national phase in: |
Ref country code: JP |
|
WWW | Wipo information: withdrawn in national office |
Country of ref document: JP |