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AU643039B2 - Improved process for removing coatings from sensitive substrates, and blasting media useful therein - Google Patents

Improved process for removing coatings from sensitive substrates, and blasting media useful therein

Info

Publication number
AU643039B2
AU643039B2 AU79828/91A AU7982891A AU643039B2 AU 643039 B2 AU643039 B2 AU 643039B2 AU 79828/91 A AU79828/91 A AU 79828/91A AU 7982891 A AU7982891 A AU 7982891A AU 643039 B2 AU643039 B2 AU 643039B2
Authority
AU
Australia
Prior art keywords
bicarbonate
blasting
hydrophobic silica
microns
media
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
AU79828/91A
Other versions
AU7982891A (en
Inventor
Lawrence Kirschner
Michael Stephen Lajoie
William E. Spears Jr.
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Church and Dwight Co Inc
Original Assignee
Church and Dwight Co Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Church and Dwight Co Inc filed Critical Church and Dwight Co Inc
Publication of AU7982891A publication Critical patent/AU7982891A/en
Application granted granted Critical
Publication of AU643039B2 publication Critical patent/AU643039B2/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B24GRINDING; POLISHING
    • B24CABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
    • B24C7/00Equipment for feeding abrasive material; Controlling the flowability, constitution, or other physical characteristics of abrasive blasts
    • B24C7/0084Equipment for feeding abrasive material; Controlling the flowability, constitution, or other physical characteristics of abrasive blasts the abrasive material being fed in a mixture of liquid and gas
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B24GRINDING; POLISHING
    • B24CABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
    • B24C1/00Methods for use of abrasive blasting for producing particular effects; Use of auxiliary equipment in connection with such methods
    • B24C1/08Methods for use of abrasive blasting for producing particular effects; Use of auxiliary equipment in connection with such methods for polishing surfaces, e.g. smoothing a surface by making use of liquid-borne abrasives
    • B24C1/086Descaling; Removing coating films
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B24GRINDING; POLISHING
    • B24CABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
    • B24C11/00Selection of abrasive materials or additives for abrasive blasts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B24GRINDING; POLISHING
    • B24CABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
    • B24C11/00Selection of abrasive materials or additives for abrasive blasts
    • B24C11/005Selection of abrasive materials or additives for abrasive blasts of additives, e.g. anti-corrosive or disinfecting agents in solid, liquid or gaseous form
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B24GRINDING; POLISHING
    • B24CABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
    • B24C7/00Equipment for feeding abrasive material; Controlling the flowability, constitution, or other physical characteristics of abrasive blasts
    • B24C7/0046Equipment for feeding abrasive material; Controlling the flowability, constitution, or other physical characteristics of abrasive blasts the abrasive material being fed in a gaseous carrier
    • B24C7/0053Equipment for feeding abrasive material; Controlling the flowability, constitution, or other physical characteristics of abrasive blasts the abrasive material being fed in a gaseous carrier with control of feed parameters, e.g. feed rate of abrasive material or carrier
    • B24C7/0061Equipment for feeding abrasive material; Controlling the flowability, constitution, or other physical characteristics of abrasive blasts the abrasive material being fed in a gaseous carrier with control of feed parameters, e.g. feed rate of abrasive material or carrier of feed pressure

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)
  • Paints Or Removers (AREA)
  • Cleaning By Liquid Or Steam (AREA)
  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
  • Detergent Compositions (AREA)

Description

TITLE: IMPROVED PROCESS FOR REMOVING COATINGS FROM SENSITIVE SUBSTRATES, AND BLASTING MEDIA USEFUL THEREIN
FIELD OF THE INVENTION
This invention relates to a process for removing coatings from sensitive metal and composite surfaces or like substrates, and to blasting media useful therein.
BACKGROUND OF THE INVENTION
It is often desirable to clean or remove coatings from the surfaces of various types of structures and equipment, varying from buildings to industrial devices. Numerous techniques are known for such purposes, ranging from mechanical abrasion techniques to the application of chemicals for cleaning or removing surface coatings such as paint, sealants, lacquers or the like. Hard, durable surfaces, such as granite walls or heavy steel plating may be cleaned or stripped by vigorous abrasive techniques such as sand blasting. More delicate surfaces may require less aggressive treatments to prevent damage to the substrates.
Both commercial airlines and military agencies spend large sums in periodically stripping or abrading paint and other coatings from the exterior surfaces of modern aircraft. These surfaces comprise light weight aluminum or other metal alloys, or composites, which are relatively soft and from which paint or other coatings must be carefully removed to avoid excessive abrasion or chemical damage. Such damage may, in extreme cases, lead to mechanical failure.
Various improved stripping techniques, similar to sand blasting, have been proposed for removing coatings from sensitive metal and composite aircraft or like surfaces. Blasting media useful for such purposes should, preferably, meet the following criteria:
1. They should be relatively non-aggressive (Mohs hardness of about 2.0-3.0) ;
2. They should be available in various particle size distributions for the treatment of different substrates;
3. They should be free-flowing under high humidity conditions and throughout a broad range of air pressure and media flow rates; and
4. They should be water soluble and non-polluting to facilitate easy separation from the insoluble paints and resins stripped to facilitate waste disposal.
Carr U.S. Patent No. 4,731,125 granted March 15, 1988 describes the use of plastic media for the blast cleaning of sensitive metal and composite surfaces. Such materials are however, relatively expensive, and their use may impose waste disposal problems.
Sodium bicarbonate has also been proposed as a blasting medium for removing coatings from sensitive substrates such as aircraft parts. Bicarbonate is an ideal choice for such a medium since it readily meets criteria 1, 2 and 4 above. Thus, it is relatively non-aggressive (Mohs hardness of about 2.5), is available in a variety of particle sizes, and is both water soluble and commonly utilized to treat sewage treatment facilities for the control of alkalinity and pH. The mild abrasive characteristics of sodium bicarbonate have previously been utilized, for example, in polishing media for teeth. See, for example, U.S. Patents Nos. 3,882,638; 3,972,123; 4,174,571; 4,412,402; 4,214,871; 4,462,803; 4,482,322; 4,487,582; 4,492,575; 4,494,932, and 4,522,597.
The principal disadvantage attendant to the use of sodium bicarbonate as a blasting medium is its tendency to cake either by compaction or, more importantly, by exposure to high humidity conditions. This is particularly acute in commercial blasting operations, the compressed air streams for which are substantially saturated with moisture, i.e., have 90% or higher relative humidities, and contain oily contaminants from air compressors. In addition, commercially available sodium bicarbonate products have intrinsically poor flow characteristics due to their normal particle size distributions and crystal shapes.
The addition of flow aids to sodium bicarbonate to improve its flow and anti-caking properties is known. Thus, the blending of tricalciu phosphate (TCP) with sodium bicarbonate in baking formulas and dental air jet prophylaxis media has previously been proposed. The addition of such material substantially improves the flow and anti-caking characteristics of the bicarbonate. TCP-treated sodium bicarbonate is however, restricted to a 3 to 6 month shelf life under ambient conditions, since the TCP absorbs moisture until saturated, after which the product cakes.
It is, accordingly, among the objects of the present invention to provide bicarbonate-containing blasting media, and a process utilizing such media for removing coatings from sensitive metal and composite surfaces. Bicarbonate blasting media which may be so utilized are free flowing and have long storage lives under adverse commercial blasting conditions, and may be utilized as blasting media at high humidities and under a broad range of finely controlled, high flow rates and air pressures. Other objects and advantages of the invention will be apparent from the following description of preferred forms thereof. SUMMARY OF THE INVENTION
In accordance with this invention, a process for removing coatings from sensitive substrates is provided, comprising blasting such surfaces with a high velocity fluid stream, desirably a substantially saturated compressed air stream under a pressure of about 10-150 psi, containing as a blasting medium crystalline water-soluble bicarbonate particles having average particle sizes within the range of about 100-500, preferably about 250-300, microns, desirably in admixture with at least about 0.2%, preferably about 0.2-3%, of a hydrophobic silica flow/anti-caking agent, by weight of the bicarbonate.
The relatively large particle size bicarbonate has been found quite effective in removing corrosion by-products as well as other coatings from substrates, without damage to the substrate. This contravenes the conventional wisdom that small particles of a blasting medium, which have more available surface area, are more effective cleaning agents than larger particles. Moreover, in most prior blasting applications higher feed rates of the blasting material lead to higher production rates, i.e., faster removal of the coating. However, employing the crystalline bicarbonate medium within the indicated particle size range it is possible to achieve economical production rates at feed rates of about three to four pounds per minute using conventional sand blasting equipment sized to effectively use a 0.5 inch diameter nozzle. Above these rates, very little increase in production rate is obtained even employing markedly higher bicarbonate blasting medium feed rates.
In accordance with a further feature of the invention, the addition of hydrophobic silica to the blasting medium imparts significantly better flow characteristics than comparable media which are either free of flow aids or which contain other conventional flow aids such as TCP or hydrophilic silica. In addition, bicarbonate blasting media incorporating the hydrophobic silica flow aid have significantly longer, substantially indefinite shelf lives, and exhibit superior resistance to the high relative humidities of commercial compressed air streams.
It is preferred to utilize crystalline sodium bicarbonate as the abrasive material in the blasting media of this invention. It is, however, intended that other crystalline water-soluble bicarbonates, e.g., alkali metal bicarbonates such as potassium bicarbonate, or ammonium bicarbonate may similarly be employed. Accordingly, while the following description principally refers to the preferred crystalline sodium bicarbonate-containing blasting media, it will be understood that the invention embraces blasting media incorporating other water-soluble crystalline bicarbonate abrasives as well.
Hydrophobic silica has previously been utilized in admixture with hydrophilic silica as a flow aid in polishing media for dental prophylaxis. Such media are applied under conditions which differ dramatically from commercial blasting media. Thus, dental prophylaxis media contain bicarbonate particles having particle sizes of about 65-70 microns, and are applied at rates of about 3 grams per minute through 1/16-1/32 inch nozzles under the pressure of clean, laboratory compressed air supplies under pressures of about 50-100 psi. Most important, such air supplies are not substantially saturated with moisture, and present quite different flow and caking problems from those inherent in the application of commercial blasting media at high thruputs in saturated compressed air blast streams.
The blasting media of the invention consist essentially of the crystalline water-soluble bicarbonate, e.g., sodium bicarbonate, in admixture with hydrophobic silica particles. Hydrophobic silica, unlike known hydrophilic silicas, is substantially free of non-hydrogen bonded silanol groups and absorbed water.
One preferred hydrophobic silica which may be utilized in the blasting media hereof is Aerosil R 972, a product which is available from Degussa AG. This material is a pure coagulated silicon dioxide aerosol, in which about 75% of the silanol groups on the surface thereof are chemically reacted with dimethyldichlorosilane, the resulting product having about 0.7 mmol of chemically combined methyl groups per 100m 2 of surface area and contai.ni.ng about 1% carbon. Its particles vary in diameter between about 10-40 nanometers and have a specific
2 surface area of about 110 m /gram. It may be prepared by flame hydrolysis of a hydrophilic silica as more fully described in Angew. Chem. 22., 744
(1960); F-PS 1,368,765; and DT-AS 1,163,784.
Further details respecting such material are contained in the technical bulletin entitled "Basic
Characteristics and Applications of AEROSIL",
Degussa AG, August 1986.
The hydrophobic silica particles are admixed with the crystalline sodium bicarbonate blasting agent in the proportion of at least about 0.2%, and up to about 3% by weight thereof. The crystalline bicarbonate particles may be of any desired average particle size, within the range of from about 100 to 500 microns. Preferably, when the blasting medium is utilized for the removal of paint from exterior aircraft surfaces, it is preferred to utilize crystalline bicarbonate particles having average particle sizes of about 250-300 microns.
Blasting media thus constituted are useful for cleaning or de-coating sensitive metals, e.g., aluminum or aluminum alloys, or composite substrates, such as utilized on exterior aircraft surfaces, without abrading or otherwise damaging the substrates. Composites which can be treated with the blasting media hereof comprise matrices, e.g., epoxy resins, which may contain fibers such as glass strands, graphite or the like for reinforcement.
The blasting medium thus constituted is preferably applied in commercial compressed air streams, i.e., streams which are substantially saturated with moisture (90% or higher relative humidities) and contain oil contaminants from compressors. A stream of water may be added to the media/air stream to cool the workpiece and control dust formation, although the addition of water may reduce the coating removal rate somewhat. The bicarbonate/hydrophobic silica blasting medium may be applied at flow rates of about 1-10, desirably about three to four, pounds per minute and under air pressures of about 10-150 psi, from 1/4 inch or larger blasting nozzles.
As indicated above, and as more fully documented below, in accordance with the present invention it has been found that blasting media so constituted and employed do not cake, have excellent shelf lives, and are free-flowing. They may thus be readily employed in commercial blasting operations for removing coatings from sensitive metal and composite surfaces.
BRIEF DESCRIPTION OF THE DRAWINGS
Figure 1 is an electron scanning photomicrograph of a clad aluminum test panel which has visible corrosion at the surface, penetrating the cladding, prior to blasting;
Figure 2 is an electron scanning photomicrograph of a clad aluminum test panel which has been cleaned according to the process of the invention. It is apparent that the surface corrosion by-product materials have been removed without damaging the metal surface; and
Figure 3 is a graph comparing production rates obtained employing bicarbonate blasting media having different average particle sizes, at varying feed rates. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The following examples illustrate the free-flowing characteristics of (Example 1), and the high production rates obtained by (Examples 2 and 3), the blasting media of the present invention. In the examples, all parts and percentages are given by weight and all temperatures in °F unless otherwise indicated.
EXAMPLE 1 Two crystalline sodium bicarbonate samples, each having an average particle size of about 250-300 microns, and one in admixture with 0.5% Aerosil R-972 hydrophobic silica, were used as media in a standard sand blasting apparatus. The apparatus was a Schmidt Accustrip System, manufactured by Schmidt Manufacturing, Inc. of Houston, Texas, having a 0.5 inch nozzle diameter and a Thompson valve connected to a 6 cubic foot blast pot and an 800 cfm compressor. The blast pot was mounted on a scale so that media flow rates could be determined.
The respective bicarbonate formulations were blasted through the nozzle at 60 psig pressure utilizing ambient compressed air which was saturated with moisture as it passed through the blasting media in the blast pot.
The crystalline sodium bicarbonate particles absent the hydrophobic silica flow aid flowed intermittently through the system, rapidly clogging the nozzle and preventing further flow. Sustained flow could not be maintained.
The crystalline bicarbonate-hydrophobic silica formulation flowed continuously through the system for more than 65 hours at controllable rates varying from 1 pound per minute to 5 pounds per minute. No flow problems were encountered therewith.
EXAMPLE 2
Test panels of aluminum, two feet by two feet by 0.032 inch thick, were cleaned by treating with water, washing with phosphoric acid solution, rinsing with water, applying Alodyne corrosion inhibitor, and rinsing with a final water rinse. An epoxide primer was applied and the panels were dried in air for eight hours. A polyurethane paint was then applied and the panels were dried for seven days. The panels were then aged for 96 hours in an air oven at 210°F. The target thickness for the paint and primer was 2 mils.
Various sodium bicarbonate blasting media were loaded into a blast pot fitted with an appropriate orifice plate to regulate the rate of flow of the blast medium. The blasting media consisted of 99.5% sodium bicarbonate (in differing particle sizes) and 0.5% Aerosil E972 hydrophobic silica. The nozzle pressure was set at 60 psi and -li¬
the media were placed under differential pressure sufficient to give the desired feed rate. The water pressure was set at a pressure of 200 psi, yielding a flow of 0.5 gal/min. The angle blast nozzle made with the workpiece was set at 60°. The media feed rates were varied from two to four lbs/min.
The time to completely depaint the panels were recorded.
The production rates and average particle sizes of the bicarbonates in the respective media were as follows:
Average Blasting Medium Abrasive Particle Size Production Rate
Crystalline NaHC03 Compacted NaHC03
Particle Size, microns _ \ ~ 2fi l≤fi 250
Production Rates (Depaintiπp Times) Feed Rate 2 lb./m n .75 1.3 1.4 1.6 Feed Rate 3 lb./min 1.0 1.7 1.8 2.0 Feed Rate 4 lb./m n 1.2 1.9 2.0 2.2
This data is summarized in Figure 3, wherein curve 1 is 2 lbs/min; curve 2 is 3 lb/min; and curve 3 is 4 lb/min.
The data shows that media incorporating the larger sodium bicarbonate average particle sizes (150 and 250 microns) were more effective at all feed rates than media containing smaller particles. It is also apparent that economical production is achieved at a medium flow rate of about three pounds per minute and that higher feed rates produce little improvement in production rate.
EXAMPLE 3
The blasting medium described in Example 1, incorporating a crystalline sodium bicarbonate having an average particle size of about 250-300 microns, in admixture with 0.5% Aerosil R-972 hydrophobic silica, was compared with a blasting medium incorporating a compacted bicarbonate, having particles in the range of -20 mesh to +40 mesh, in admixture with a like amount (0.5%) of the same hydrophobic silica flow aid. The respective media were utilized to depaint aluminum test panels in the manner described in Example 2. The maximum production rates obtained with the respective media were determined, and are tabulated below. The tabulation shows the improved production rate achieved using the blasting medium incorporating the crystalline sodium bicarbonate rather than the medium incorporating the compacted sodium bicarbonate:
Average
Blasting Medium Abrasive Particle Size Production Rate
2 microns ft. /min
Crystalline NaHC03 275 2.2
Compacted NaHC03 390 1.0
From the preceding disclosure, it will be seen that the present invention provides an improved process for cleaning or removing paint or other coatings from the surfaces of sensitive substrates, and to crystalline sodium bicarbonate-containing blasting media useful therein. It will be understood that various changes may be made in the blasting process and blasting media exemplified in the preferred embodiments described hereinabove without departing from the scope of the invention. Accordingly, the preceding description should be construed as illustrative and not in a limiting sense.

Claims

We claim:
1. A process for removing coatings from sensitive metal and composite surfaces, which comprises blasting said surfaces with a high velocity fluid stream containing as a blasting medium water-soluble crystalline bicarbonate particles selected from the group consisting of alkali metal and ammonium bicarbonates, said bicarbonate particles having average particle sizes within the range of 100-500 microns.
2. The process of claim 1, wherein the fluid stream is a substantially saturated compressed air stream under pressures of 10-150 psi.
3. The process of claim 1, wherein the blast stream is applied to the surface treated at a rate of 1-10 pounds of the bicarbonate particles per minute.
4. The process of claim 1, wherein the bicarbonate particles have an average particle size within the range of 250-300 microns.
5. The process of claim 1, wherein the bicarbonate is sodium bicarbonate.
6. The process of claim 1, wherein the blasting medium contains 0.2-3% by weight of the bicarbonate, of a hydrophobic silica flow/anti-caking agent.
7. The process of claim 6, wherein the hydrophobic silica is substantially free of non-hydrogen bonded silanol groups and adsorbed water.
8. A blasting medium for removing coatings from sensitive metal and composite surfaces, which consists essentially of water-soluble crystalline bicarbonate particles selected from the group consisting of alkali metal and ammonium bicarbonates, said bicarbonate particles having average particle sizes within the range of 100-500 microns, in admixture with from 0.2% to 3% by weight of the bicarbonate, of a hydrophobic silica flow/anti-caking agent.
9. The blasting medium of claim 8, wherein the bicarbonate is sodium bicarbonate, and the hydrophobic silica is substantially free of non-hydrogen bonded silanol groups and adsorbed water.
10. The blasting medium of claim 8, wherein the bicarbonate particles have an average particle size within the range of 250-300 microns.
AU79828/91A 1990-04-06 1991-04-04 Improved process for removing coatings from sensitive substrates, and blasting media useful therein Ceased AU643039B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US50644790A 1990-04-06 1990-04-06
US506447 1990-04-06

Publications (2)

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AU7982891A AU7982891A (en) 1991-10-30
AU643039B2 true AU643039B2 (en) 1993-11-04

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EP (1) EP0525122A4 (en)
JP (1) JPH0669668B2 (en)
KR (1) KR960003113B1 (en)
CN (1) CN1029599C (en)
AU (1) AU643039B2 (en)
CA (1) CA2079892C (en)
MY (1) MY109653A (en)
NO (1) NO176751C (en)
NZ (1) NZ237596A (en)
PL (1) PL165174B1 (en)
TR (1) TR25589A (en)
WO (1) WO1991015308A1 (en)

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US5232514A (en) * 1991-10-10 1993-08-03 Church & Dwight Co., Inc. Corrosion-inhibiting cleaning systems for aluminum surfaces, particularly aluminum aircraft surfaces
WO1993018863A1 (en) * 1992-03-20 1993-09-30 Church & Dwight Company, Inc. Abrasive coating remover and process for using same
US5593339A (en) * 1993-08-12 1997-01-14 Church & Dwight Co., Inc. Slurry cleaning process
NL1003398C2 (en) * 1996-06-21 1997-12-23 Delwi Ontwikkelingen B V Passage-wall cleaning system using granular material
US6010546A (en) * 1997-07-24 2000-01-04 Asahi Glass Company, Ltd. Blasting medium and blasting method employing such medium
NL1007501C2 (en) * 1997-11-10 1999-05-11 Pieter Schurink Cleaning surfaces by blasting to remove e.g. dirt, scale or paint
DE19842053A1 (en) 1998-09-15 2000-03-23 Bayer Ag Use of polyaspartic acids in cleaning formulations with an abrasive effect
DE19842054A1 (en) 1998-09-15 2000-03-16 Bayer Ag Use of water-soluble polymeric polycarboxylates in cleaning formulations with an abrasive effect
GB2565122A (en) * 2017-08-03 2019-02-06 Rolls Royce Plc Gas turbine engine
FR3102694B1 (en) 2019-10-30 2022-06-03 Safran Aircraft Engines PROCESS FOR COMPACTING AN ANTI-CORROSION COATING
CN111673622A (en) * 2020-06-01 2020-09-18 江苏佰健环保科技有限公司 Environment-friendly cleaning process and equipment for food utensil non-stick coating
CN113996602A (en) * 2021-11-02 2022-02-01 东南大学 A kind of hole drilling and dirt cleaning method of printed circuit board

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Publication number Publication date
TR25589A (en) 1993-07-01
KR960003113B1 (en) 1996-03-05
CA2079892C (en) 1996-01-23
NO923823D0 (en) 1992-10-01
CN1056077A (en) 1991-11-13
NO176751C (en) 1995-05-24
NO176751B (en) 1995-02-13
JPH05504919A (en) 1993-07-29
NO923823L (en) 1992-11-30
AU7982891A (en) 1991-10-30
WO1991015308A1 (en) 1991-10-17
PL165174B1 (en) 1994-11-30
EP0525122A1 (en) 1993-02-03
JPH0669668B2 (en) 1994-09-07
CN1029599C (en) 1995-08-30
NZ237596A (en) 1993-03-26
CA2079892A1 (en) 1991-10-07
EP0525122A4 (en) 1993-04-28
MY109653A (en) 1997-03-31

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