EP0832719B1 - Wet-blast installation - Google Patents
Wet-blast installation Download PDFInfo
- Publication number
- EP0832719B1 EP0832719B1 EP97109332A EP97109332A EP0832719B1 EP 0832719 B1 EP0832719 B1 EP 0832719B1 EP 97109332 A EP97109332 A EP 97109332A EP 97109332 A EP97109332 A EP 97109332A EP 0832719 B1 EP0832719 B1 EP 0832719B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- propellant
- granulate
- liquid
- pressure vessel
- installation according
- 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.)
- Expired - Lifetime
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B24—GRINDING; POLISHING
- B24C—ABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
- B24C7/00—Equipment for feeding abrasive material; Controlling the flowability, constitution, or other physical characteristics of abrasive blasts
- B24C7/0084—Equipment 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B24—GRINDING; POLISHING
- B24C—ABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
- B24C5/00—Devices or accessories for generating abrasive blasts
- B24C5/02—Blast guns, e.g. for generating high velocity abrasive fluid jets for cutting materials
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B24—GRINDING; POLISHING
- B24C—ABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
- B24C7/00—Equipment for feeding abrasive material; Controlling the flowability, constitution, or other physical characteristics of abrasive blasts
- B24C7/0046—Equipment for feeding abrasive material; Controlling the flowability, constitution, or other physical characteristics of abrasive blasts the abrasive material being fed in a gaseous carrier
- B24C7/0053—Equipment 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B24—GRINDING; POLISHING
- B24C—ABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
- B24C7/00—Equipment for feeding abrasive material; Controlling the flowability, constitution, or other physical characteristics of abrasive blasts
- B24C7/0046—Equipment for feeding abrasive material; Controlling the flowability, constitution, or other physical characteristics of abrasive blasts the abrasive material being fed in a gaseous carrier
- B24C7/0076—Equipment for feeding abrasive material; Controlling the flowability, constitution, or other physical characteristics of abrasive blasts the abrasive material being fed in a gaseous carrier the blasting medium being a liquid stream
Definitions
- the present invention relates on a wet blasting system with two controllable system parts, one of which is a controllable facility part of the deployment of dry granules in a gaseous blowing agent is suspended, serves and the other controllable part of the system the provision of a mixture of gaseous propellants and granules to be mixed liquid, the Mixture of granulate and blowing agent on the one hand and liquid on the other hand, to be assigned to an operator Spray tool is done.
- the object of the invention is such a wet blasting system to train that so-called bridging in the granule boiler and thus a disturbance of the Operating sequence is prevented.
- the solution to this problem is the formation of a wet blasting system with the aforementioned features such that the first controllable system part a compressor to form the Blowing agent in the form of compressed gas, a granulate heater between the compressor and a pressure vessel Granulate storage and an introduction of the compressed gas into the Pressure vessel to form the dosed to be removed Has granules / blowing agent mixture, while the second controllable system part of a high pressure pump to promote the Liquid between a liquid supply source and the Spray tool is used, cooling the compressor coming gaseous blowing agent takes place in two heat exchangers, which the gaseous propellant between the compressor and pressure vessel is fed in succession, and of which the the first is the granulate heating of the first part of the system, so that in it a heating of the granulate / blowing agent mixture leaving the pressure vessel and cooling the blowing agent or compressed gas takes place while in the second heat exchanger Heat exchange between that of the liquid supply source coming and the liquid to be sprayed on the one hand and the propellant to be
- W0 94/21426 already describes a wet blasting system two parts of the system, one part of the system one Compressed air supply, which by means of a delivery line is connected to a jet nozzle, in which Delivery line between compressed air supply and jet nozzle the air is dried and the pressure is regulated and granules in front of the jet nozzle of the conveyed compressed air is mixed from one granulate store while the other Plant part a pump for pumping water from a Water reservoir for the jet nozzle and for mixing from water to the compressed air granulate mixture in the jet nozzle includes, with the water reservoir as a heat exchanger is formed in which the pump Warm water and one coming from the compressed air supply Compressed air portion is cooled accordingly before this Increasing the air pressure in the granulate storage in this Granulate storage is fed.
- its aim is that dry granulate provided by one part of the plant, suspended according to the invention in a gaseous blowing agent and that provided by the other part of the system Bring liquid together so that the necessary Control operations performed by a single operator can be.
- a gaseous blowing agent provided by the other part of the system Bring liquid together so that the necessary Control operations performed by a single operator can be.
- One is used to achieve this goal further embodiment of the wet blasting system according to the invention such that the control of both parts of the system centrally from Spray tool is carried out by the operator to be actuated signal transmitter for control means in the respective are assigned to both parts of the system.
- the one pressure vessel 3 and one 4 includes.
- the moist warm compressed air supplied to a heat exchanger 5 the Cold water supplied as coolant via a line 6 is, the heat exchanger 5 as hot water via a line 7 leaves.
- the heat exchanger 5 is a countercurrent principle working water powered air cooler. compressed air and from it precipitated in the heat exchanger or air cooler 5 Condensate enters a water separator 8 which the condensate is drained off, so that the remaining Air as dry compressed air via line 9 into the pressure vessel 3 arrives.
- the arrow 10 is the input of the granules shown in the pressure vessel 3.
- Granulate is a subset of the pressure vessel taken, the amount withdrawn by means of a granulate metering valve 11 can be determined.
- Granulate subsets arrive in steady succession in the pellet heating 4, in the one Part of the dry compressed air provided according to Fig.l. arrives.
- the total amount of dry compressed air comes over the line 9 already mentioned in connection with FIG. 1 via a compressed air control valve 12 to a branch point 13, from which a first subset via the line 14 into the granulate heater 4 and a second subset, is the dry compressed air, which is shown in FIG. 1 in the pressure vessel 3 arrives.
- the relationship between the first and second Partial quantity is by means of a conveying air control valve 14 in line branch 15 from branching point 13 to granule heating 4 determined.
- the mixture of granules and drier Compressed air in an appropriate amount and in an appropriate ratio between the mixture components is called compressed air blasting media mixture (Arrow 16) of the blasting gun 17.
- FIG. 3 The way of process water as the preferred dust-binding Liquid is shown in Fig. 3.
- a source of water 18 in water tank or connecting a water pipe cold water (arrow 19) is removed and the heat exchanger or water-operated air cooler 5 fed to be used in it as above has been described in connection with FIG. 1. That about the Line 7 leaving the heat exchanger or air cooler 5 Hot water (represented by arrow 20) is by means of a pneumatic high pressure pump 21 of the blasting gun 17 fed.
- a 12 volt current is drawn from the compressor battery 22, to be fed to a switch and control panel 23, from which the power supply of the conveying air control valve 14 (electrical line 24), the pneumatic high-pressure pump 21 (electrical line 25) and the granulate metering valve 11 (electrical line 26) is effected. Furthermore, the switch and control panel 23 Supply of a dead man circuit 27 (electrical line 28) and a boiler vibrator 29 (electrical line 30) causes.
- the dead man circuit 27 is before the branch point 13 downstream of the compressed air control valve 12. As soon as the Influence of the operator of the system on the blasting gun 17 ceases, the function of the entire system terminated by stopping the supply of dry compressed air,
- the boiler vibrator is one around the outlet 31 of the pressure boiler placed vibrator 32 of suitable design.
- 32 should be used as an additional safeguard against bridging, especially since they only intended as an additional safeguard against bridging is correspondingly simple and can be trained external assignment to the boiler outlet 31 a simple monitoring and any necessary repairs with the least possible Disruption of the operational sequence makes possible.
- Fig. 5 is the overall system with the way of the process water 3, the path of the compressed air according to FIG. 1 and the Away from conveying air and blasting media according to FIG. 2 as a block diagram shown.
- the reference numerals are used, which are also in FIGS. 1 to 3 have been used so that the paths of water (arrow 20) and granules fluidized in compressed air (arrow 16) to the spray gun 17 can be understood without this in individual would have to be described again.
- trained signal transmitter line 31 Fig.
- the spray gun 17 itself is not actually Object of the present invention, except for the accommodation of the keyboard or switch board, which, however, basically can be done in any way. It will consequently from the description of the spray gun in detail apart from and referring to Fig. 6, the internal structure the spray gun shows.
- Fig. 5 the vibrating device 29 is shown as arranged in the boiler 3; in fact, according to FIG. 2, it should be the area of the outside Surround boiler outlet 11.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Nozzles (AREA)
- Agricultural Chemicals And Associated Chemicals (AREA)
- Catching Or Destruction (AREA)
- Fertilizers (AREA)
- Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
Abstract
Description
Bei der Reinigung von gegliederten Gebäudefassaden, von Steinskulpturen und ähnlichen Gegenständen sind eine ganze Reihe von Bedingungen zu beachten, die sich teilweise aus der Sachanforderung ergeben, den zu behandelnden Gegenstand von nicht wünschenswerten, teilweise hartnäckigen Ablagerungen zu befreien, ohne ihn zu zerstören, die sich aber auch teilweise aus Vorschriften ergeben, die mit dem Umweltschutz und dergleichen begründet werden. So wäre es beispielsweise möglich, einen Gegenstand im Sinn der Ausgangssituation der vorliegenden Erfindung schonend, effizient und wirtschaftlich von insbesondere aus der Umweltbelastung resultierenden Ablagerungen durch ein Granulat zu befreien, das in einem energiereichen Druckluftstrom suspendiert ist. Es müßten lediglich Druck und Mischungsverhältnis zwischen Druckluft und Granulat "richtig" eingestellt werden. Dabei fällt selbstverständlich in erheblichem Maße Staub an, der als Umweltbelastung, zumindest aber als Umweltbelästigung empfunden wird, weshalb trotz durchaus möglicher Schutzmaßnahmen diese "Trockensandstrahlung" vielfach nicht zugelassen ist und das "Naßsandstrahlen" eingesetzt werden muß. Der Suspension aus Treibgas und Granulat muß dabei eine Flüssigkeit zugemischt werden, um den beim "Sandstrahlen" anfallenden Staub zu binden. When cleaning structured building facades, from Stone sculptures and similar objects are a whole Note a number of conditions, some of which arise from result from the factual request, the object to be treated of undesirable, sometimes stubborn deposits to free it without destroying it, but the also partially resulting from regulations related to environmental protection and the like are justified. For example, it would be possible an object in the sense of the initial situation the present invention gentle, efficient and economical of those resulting in particular from environmental pollution To remove deposits by a granulate, which in one high-energy compressed air flow is suspended. It should be only pressure and mixing ratio between compressed air and granules are set "correctly". It goes without saying to a significant extent dust that is considered an environmental pollution, at least perceived as an environmental nuisance why, despite possible protective measures "Dry sandblasting" is often not permitted and the "wet sandblasting" must be used. The suspension A liquid must be added from the propellant and granules in order to avoid the dust generated by "sandblasting" to tie.
In diesem Zusammenhang bezieht sich die vorliegende Erfindung auf eine Naßstrahlanlage mit zwei steuerbaren Anlagenteilen, von denen der eine steuerbare Anlagenteil der Bereitstellung von trockenem Granulat, das in einem gasförmigen Treibmittel suspendiert ist, dient und der andere steuerbare Anlagenteil der Bereitstellung einer dem Gemisch aus gasförmigem Treibmittel und Granulat zuzumischenden Flüssigkeit dient, wobei die Mischung von Granulat und Treibmittel einerseits und Flüssigkeit andererseits in einem einer Bedienungsperson zuzuordnenden Sprühwerkzeug erfolgt.In this context, the present invention relates on a wet blasting system with two controllable system parts, one of which is a controllable facility part of the deployment of dry granules in a gaseous blowing agent is suspended, serves and the other controllable part of the system the provision of a mixture of gaseous propellants and granules to be mixed liquid, the Mixture of granulate and blowing agent on the one hand and liquid on the other hand, to be assigned to an operator Spray tool is done.
Aufgabe der Erfindung ist es, eine solche Naßstrahlanlage so auszubilden, dass eine sogenannte Brückenbildung im Granulat- Kessel und damit eine hierdurch verursachte störung des Betriebsablaufes verhindert wird.The object of the invention is such a wet blasting system to train that so-called bridging in the granule boiler and thus a disturbance of the Operating sequence is prevented.
Der Lösung dieser Aufgabe dient die Ausbildung einer Naßstrahlanlage mit den vorgenannten Merkmalen derart, dass der erste steuerbare Anlagenteil einen Kompressor zur Bildung des Treibmittels in der Form von Druckgas, eine Granulatheizung zwischen Kompressor und einem als Druckkessel ausgebildeten Granulatspeicher und eine Einleitung des Druckgases in den Druckkessel zur Bildung des diesem dosiert zu entnehmenden Granulat/Treibmittelgemisches aufweist, während der zweite steuerbare Anlagenteil einer Hochdruckpumpe zur Förderung der Flüssigkeit zwischen einer Flüssigkeitsvorratsquelle und dem Sprühwerkzeug dient, wobei eine Kühlung des vom Kompressor kommenden gasförmigen Treibmittels in zwei Wärmetauschern erfolgt, denen das gasförmige Treibmittel zwischen Kompressor und Druckkessel nacheinander zugeführt wird, und von denen der erste die Granulatheizung des ersten Anlageteils ist, sodass in ihm ein Aufheizen des den Druckkessel verlassenden Granulat/Treibmittelgemisches und eine Kühlung des Treibmittels bzw.Druckgases erfolgt, während im zweiten Wärmetauscher ein Wärmetausch zwischen der von der Flüssigkeitsvorratsquelle kommenden und dem Sprühwerkzeug zuzuführenden Flüssigkeit einerseits und dem dem Druckkessel zuzuführenden Treibmittel andererseits erfolgt und das Treibmittel weiter gekühlt und getrocknet, die Flüssigkeit erwärmt.The solution to this problem is the formation of a wet blasting system with the aforementioned features such that the first controllable system part a compressor to form the Blowing agent in the form of compressed gas, a granulate heater between the compressor and a pressure vessel Granulate storage and an introduction of the compressed gas into the Pressure vessel to form the dosed to be removed Has granules / blowing agent mixture, while the second controllable system part of a high pressure pump to promote the Liquid between a liquid supply source and the Spray tool is used, cooling the compressor coming gaseous blowing agent takes place in two heat exchangers, which the gaseous propellant between the compressor and pressure vessel is fed in succession, and of which the the first is the granulate heating of the first part of the system, so that in it a heating of the granulate / blowing agent mixture leaving the pressure vessel and cooling the blowing agent or compressed gas takes place while in the second heat exchanger Heat exchange between that of the liquid supply source coming and the liquid to be sprayed on the one hand and the propellant to be supplied to the pressure vessel on the other hand takes place and the blowing agent is further cooled and dried, the liquid warms up.
W0 94/21426 beschreibt bereits eine Naßstrahlanlage mit zwei Anlagenteilen, von denen der eine Anlagenteil eine Druckluftzuführung aufweist, die mittels einer Förderleitung mit einer Strahldüse verbunden ist, wobei in diese Förderleitung zwischen Druckluftzuführung und Strahldüse eine Trocknung der Luft und eine Druckregelung erfolgt und vor der Strahldüse der geförderten Druckluft ein Granulat aus einem Granulatspeicher zugemischt wird, während der andere Anlagenteil eine Pumpe zum Fördern von Wasser aus einem Wasservorratsbehälter zur Strahldüse und zum Zumischen von Wasser zu dem Druckluft-Granulat-Gemisch in der Strahldüse einschließt, wobei der Wasservorratsbehälter als Wärmetauscher ausgebildet ist, in dem das zur Pumpe gelangende Wasser gewärmt und ein von der Druckluftzuführung kommender Druckluftanteil entsprechend gekühlt wird, ehe dieser zur Erhöhung des Luftdruckes in dem Granulatspeicher in diesen Granulatspeicher eingespeist wird.W0 94/21426 already describes a wet blasting system two parts of the system, one part of the system one Compressed air supply, which by means of a delivery line is connected to a jet nozzle, in which Delivery line between compressed air supply and jet nozzle the air is dried and the pressure is regulated and granules in front of the jet nozzle of the conveyed compressed air is mixed from one granulate store while the other Plant part a pump for pumping water from a Water reservoir for the jet nozzle and for mixing from water to the compressed air granulate mixture in the jet nozzle includes, with the water reservoir as a heat exchanger is formed in which the pump Warm water and one coming from the compressed air supply Compressed air portion is cooled accordingly before this Increasing the air pressure in the granulate storage in this Granulate storage is fed.
Bei einer erfindungsgemäß ausgebildeten Naßstrahlanlage wird in höchstem Maße die Gefahr der Brückenbildung im Granulatkessel ausgeschaltet .In a wet blasting system designed according to the invention to the greatest extent the danger of Bridge formation in the granulate boiler switched off.
In weiterer Ausgestaltung der Erfindung ist es ihr Ziel, das durch den einen Anlageteil bereitgestellte trockene Granulat, das erfindungsgemäß in einem gasförmigen Treibmittel suspendiert ist, und die durch den anderen Anlageteil bereitgestellte Flüssigkeit so zusammenzubringen, dass die notwendigen Steuervorgänge von einer einzigen Bedienungsperson durchgeführt werden können. Der Erreichung dieses Zieles dient eine weitere Ausgestaltung der erfindungsgemäßen Naßstrahlanlage derart, dass die Steuerung beider Anlageteile zentral vom Sprühwerkzeug aus erfolgt, dem hierzu von der Bedienungsperson zu betätigende Signalgeber für Steuermittel im jeweiligen der beiden Anlageteile zugeordnet sind.In a further embodiment of the invention, its aim is that dry granulate provided by one part of the plant, suspended according to the invention in a gaseous blowing agent and that provided by the other part of the system Bring liquid together so that the necessary Control operations performed by a single operator can be. One is used to achieve this goal further embodiment of the wet blasting system according to the invention such that the control of both parts of the system centrally from Spray tool is carried out by the operator to be actuated signal transmitter for control means in the respective are assigned to both parts of the system.
Während für die Bedienung bisher im Einsatz befindlicher Naßstrahlanlagen mindestens zwei Bedienungsperonen notwendig waren, reicht für die Bedienung einer erfindungsgemäßen Naßstrahlanlage eine Bedienungsperson aus.While for the operation of previously used wet blasting systems at least two operators were necessary, is sufficient for the operation of a wet blasting system according to the invention an operator.
Weitere zweckmäßige Merkmale zur Weiterbildung der Erfindung ergeben sich aus den Ansprüchen, wie sie nachfolgend anhand der Zeichnung erläutert werden. In der Zeichnung zeigen:
- Fig. 1
- als Blockschaltbild das Anlagenkonzept,
- Fig. 2
- wiederum als Blockschaltbild den Weg von Förderfluid und Strahlmittel zum Sprühwerkzeug, das nachfolgend entsprechend der allgemeinen Praxis als Strahlpistole bezeichnet wird,
- Fig. 3
- erneut als Blockschaltbild den Weg der Brauchflüssigkeit zur Strahlpistole,
- Fig. 4
- das Schema der 12-Volt-Steuerleitungen,
- Fig. 5
- das als Blockschaltbild gezeichnete Schaltbild der Gesamtanlage,
- Fig. 6
- den inneren Aufbau der Strahlpistole,
- Fig. 1
- the system concept as a block diagram,
- Fig. 2
- again as a block diagram the path of the conveying fluid and blasting agent to the spraying tool, which is referred to below as the blasting gun in accordance with general practice,
- Fig. 3
- again as a block diagram the route of the process liquid to the blasting gun,
- Fig. 4
- the scheme of the 12 volt control lines,
- Fig. 5
- the circuit diagram of the entire system drawn as a block diagram,
- Fig. 6
- the internal structure of the blasting gun,
Gemäß Fig. 1 fördert eine Druckquelle in der Form eines
Kompressors 1 feuchtwarme Druckluft als Förderfluid in eine
mit dieser Druckluft als Preßluft betriebene Granulatheizung 2
im Dosierbereich, die einen Druckkessel 3 und eine
4 einschließt. Nach Verlassen der granulat-Heizung 4 wird die
feuchtwarme Druckluft einem Wärmetauscher 5 zugeführt, dem
als Kühlmittel über eine Leitung 6 Kaltwasser zugeleitet
wird, das den Wärmetauscher 5 als Warmwasser über eine Leitung
7 verläßt. Der Wärmetauscher 5 ist ein im Gegenstromprinzip
arbeitender wasserbetriebener Luftkühler. Druckluft
und daraus im Wärmetauscher bzw. Luftkühler 5 niedergeschlagenes
Kondensat gelangen in einen Wasserabscheider 8 aus
dem das Kondensat abgeleitet wird, sodaß die verbliebene
Luft als trockene Druckluft über die Leitung 9 in den Druckkessel
3 gelangt. 1 promotes a pressure source in the form of a
Compressor 1 moist warm compressed air as a conveying fluid in a
pellet heating operated with this compressed air as compressed
In Fig. 2 ist mit dem Pfeil 10 die Eingabe des Granulats
in den Druckkessel 3 dargestellt. Aus dem im Druckkessel 3
befindlichen Granulat wird eine Teilmenge dem Druckkessel
entnommen, wobei die Entnahmemenge mittels eines Granulatdosierventils
11 bestimmbar ist. Granulatteilmengen gelangen
in stetiger Folge in die Granulatheizung 4, in die ein
Teil der gemäß Fig.l bereitgestellten trockenen Druckluft
gelangt. Die Gesamtmenge der trockenen Druckluft kommt über
die bereits im Zusammenhang mit Fig. 1 genannte Leitung 9
über ein Druckluftsteuerventil 12 an einen Verzweigungspunkt
13, von dem aus eine erste Teilmenge über die Leitung
14 in die Granulatheizung 4 und eine zweite Teilmenge,
die trockene Druckluft ist, die gemäß Fig. 1 in den Druckkessel
3 gelangt. Das Verhältnis zwischen erster und zweiter
Teilmenge wird mittels eines Förderluftstellventiles 14
im Leitungszweig 15 vom Verzweigungspunkt 13 zur Granulatheizung
4 bestimmt. Das Gemisch aus Granulat und trockener
Druckluft in angemessener Menge und angemessenem Verhältnis
zwischen den Gemischkomponenten wird als Druckluft-Strahlmittelgemisch
(Pfeil 16) der Strahlpistole 17 zugeführt.In Fig. 2, the
Der Weg des Brauchwassers als bevorzugter staubbindender
Flüssigkeit ist in Fig. 3 dargestellt. Einer Wasservorratsquelle
18, die in Wassertank oder der Anschluß einer Wasserleitung
sein kann, wird Kaltwasser (Pfeil 19) entnommen
und dem Wärmetauscher bzw. wasserbetriebenen Luftkühler 5
zugeführt, um darin so eingesetzt zu werden, wie es oben
im Zusammenhang mit Fig. 1 beschrieben wurde. Das über die
Leitung 7 den Wärmetauscher bzw. Luftkühler 5 verlassende
Warmwasser (dargestellt durch den Pfeil 20) wird mittels
einer pneumatischen Hochdruckpumpe 21 der Strahlpistole 17
zugeführt.The way of process water as the preferred dust-binding
Liquid is shown in Fig. 3. A source of
Der Kompressorbatterie 22 wird ein 12-Volt-Strom entnommen,
um einem Schalt- und Steuerpult 23 zugeleitet zu werden,
von dem aus die Stromversorgung des Förderluftstellventiles
14 (elektrische Leitung 24), der pneumatischen Hochdruckpumpe
21 (elektrische Leitung 25) und des Granulatdosierventils
11 (elektrische Leitung 26) bewirkt wird.
Des weiteren wird vom Schalt- und Steuerpult 23 aus die
Versorgung einer Totmannschaltung 27 (elektrische Leitung
28) und eines Kesselrüttlers 29 (elektrische Leitung
30) bewirkt.A 12 volt current is drawn from the
Die Totmannschaltung 27 ist dem Verzweigungspunkt 13 vorund
dem Druckluftstellventil 12 nachgeschaltet. Sobald die
Einwirkung der Bedienungsperson der Anlage auf die Strahlpistole
17 aufhört, wird die Funktion der gesamten Anlage
durch Beendigung der Zuführung der trockenen Druckluft beendet,The
Der Kesselrüttler ist eine außen um den Auslaß 31 des Druck-kessels
gelegte Rütteleinrichtung 32 geeigneter Ausgestaltung.
Dadurch, daß der Druckkessel 3 mit trockener Druckluft
beschickt wird, ist die Gefahr von Brückenbildung vor dem
Auslaß 31 des Druckkessels 3 zwar minimiert, aber die Rütteleinrichtung
32 sollte vorsorglich als zusätzliche Sicherung
gegen Brückenbildung vorgesehen sein, zumal sie, weil sie
nur als zusätzliche Sicherung gegen Brückenbildung gedacht
ist, entsprechend einfach ausgebildet werden kann und ihre
äußere Zuordnung zum Kesselauslaß 31 eine einfache Überwachung
und gegebenenfalls notwendige Reparatur bei geringstmöglicher
Störung des Betriebsablaufs möglich macht. The boiler vibrator is one around the
In Fig. 5 ist die Gesamtanlage mit dem Weg des Brauchwassers
gemäß Fig. 3, dem Weg der Preßluft gemäß Fig. 1 sowie dem
Weg von Förderluft und Strahlmittel gemäß Fig. 2 als Blockschaltbild
dargestellt. Für gleiche Komponenten der Anlage
sind die Bezugszeichen verwendet, die auch in Fig. 1 bis 3
verwendet worden sind, sodaß die Wege von Wasser (Pfeil 20)
und in Druckluft fluidisiertem Granulat (Pfeil 16) zur Sprühpistole
17 nachvollzogen werden können, ohne daß dies im
einzelnen nochmals beschrieben werden müßte. Uber die entsprechend
ausgebildete Signalgeberleitung 31 (Fig. 4,5)
ist ein manuell zu betätigendes, in die Sprühpistole 17
eingefügtes Tastenbrett mit dem zentralen Schalt- und Steuerpult
23 derart verbunden, daß von der Bedienungsperon, die
die Sprühpistole 17 handhabt, eine Mengen- und Druckregelung
von Wasser (Pfeil 20) und Druckluft Granulat-Gemisch (Pfeil 16)
individuell und entsprechend den jeweils vorliegenden Anforderungen
möglich ist, auch wenn die Orte der Handhabung
der Sprühpistole 17 und der Aufstellung des Schalt- und
Steuerpultes 23 sowie der über diese zu bestimmenden Anlage
weit auseinander liegen, indem beispielsweise die Anlage
mit dem Schalt- und Steuerpu lt auf dem Boden vor einem
eingerüsteten Gebäude aufgestellt ist und ein Arbeiter mit
der Sprühpistole am entfertesten Punkt des Gerüstes tätig
ist.In Fig. 5 is the overall system with the way of the
Die Sprühpistole 17 selbst ist an sich nicht eigentlich
Gegenstand der vorliegenden Erfindung, ausgenommen die Unterbringung
des Tasten- bzw. Schaltbrettes, die jedoch grundsätzlich
in jeder beliebigen Weise erfolgen kann. Es wird
demzufolge von der Beschreibung der Sprühpistole im einzelnen
abgesehen und auf Fig. 6 verwiesen, die den inneren Aufbau
der Sprühpistole zeigt. The
Wesentlich ist die Auslegung der Sprühpistole derart, daß
die Zumischung der Flüssigkeit (20) zu dem Gemisch (16)
aus gasförmigem Treibmittel und Granulat in der Sprühpistole
18 erfolgt.It is essential to design the spray gun in such a way that
admixing the liquid (20) to the mixture (16)
made of gaseous propellant and granules in the
Darauf hinzuweisen ist noch, daß in Fig. 5 die Rütteleinrichtung
29 als im Kessel 3 angeordnet dargestellt ist;
tatsächlich soll sie gemäß Fig. 2 außen den Bereich des
Kesselauslasses 11 umgeben.It should also be noted that in Fig. 5 the
Claims (16)
- A wet spray installation comprising two controllable parts (16, 20), one controllable part (16) being used to prepare dry granulate suspended in a gaseous propellant and the other controllable part (20) being used for supplying a liquid for adding to the mixture of gaseous propellant and granulate, wherein the granulate and propellant on the one hand and the liquid on the other hand are mixed in a spray tool (17) assigned to an operator, wherein the first controllable part (16) comprises a compressor (1) for obtaining the propellant in the form of a compressed gas, a granulate reservoir in the form of a pressure vessel (3) and an inlet for pressure gas into the pressure vessel (3) in order to form the mixture of granulate and propellant for removal therefrom in metered manner, whereas the second controllable part is a high-pressure pump (21) for conveying the liquid between a liquid supply source (18) and the spray tool (17) and wherein heat between the gaseous propellant and the liquid is exchanged in a heat exchanger, characterised in that the heat exchange is effected in two heat exchangers (4, 5) which are successively supplied with gaseous propellant between the compressor (1) and the pressure vessel (3), and the first heat exchanger is the granulate heater (4) at the outlet of the pressure vessel (3) in the first part (16) so that the mixture of granulate and propellant leaving the pressure vessel (3) is heated therein and the propellant or pressure gas is cooled therein, whereas the second heat exchanger (5) is that in which the heat exchange is effected between the liquid coming from the supply source (18) and supplied to the spray tool (17) on the one hand and the propellant for supplying to the pressure vessel on the other hand and the propellant is additionally cooled and dried and the liquid is heated.
- A wet spray installation according to claim 1, characterised in that the two parts (16, 20) of the installation are centrally controlled by the spray tool (17), which to that end is associated with a signal transmitter actuated by the operator for control means in each of the two parts (16, 17).
- A wet spray installation according to claim 1 or 2, characterised in that a part of the dry propellant in which the granulate leaving the pressure vessel (3) is suspended is withdrawn before being introduced into the pressure vessel.
- A wet spray installation according to claim 1 or 2, characterised in that a liquid separator is disposed between the second heat exchanger (5) and the pressure vessel (3) and from it the liquid separated from the propellant in the liquid separator itself together with the liquid already separated from the propellant in the second heat exchanger (5) and supplied to the liquid separator separately from the propellant IS removed on the one hand and the dry propellant is removed on the other hand.
- A wet spray installation according to any of claims 1 to 4, characterised by a metering device (11) for the granulate at the pressure-vessel outlet (31) and a metering device (14) for determining the ratio between the quantity of dry propellant introduced into the pressure vessel (3) and the quantity of propellant suspended in the granulate, wherein the granulate downstream of the metering device (11) is suspended at the pressure vessel outlet in the propellant downstream of the second metering device (14) in a mixing chamber (4).
- A wet spray installation according to claim 5, characterised in that the liquid is added to the mixture of propellant and granulate suspended therein in the spray tool (17).
- A wet spray installation according to any of claims 1 to 6, characterised by a "dead man's off switch" (27) through which dried propellant is conveyed before being introduced into the pressure vessel (3).
- A wet spray installation according to any of claims 1 to 7, characterised by a vibrator (32) externally associated with the pressure vessel (3), mounted with little vibration, in the neighbourhood of the outlet nozzles thereof.
- A wet spray installation according to any of claims 2 to 8, characterised in that the compressor in the first part of the installation is a pump (111) driven by gaseous fluid taken from the same central supply pipe (103) from which the gaseous propellant for conveying the granulate from the pressure vessel to the spray tool (100) is taken, and a control valve (106) is provided for supplying fluid to the pump motor (110) and a second control valve (107) is provided for the granulate propellant and are operated in dependence on one another so that when a spray operation is started, only the control valve (106) for supplying fluid to the pump motor (111) is initially opened in order to supply a relatively large amount of liquid in the frame of the second part of the installation for supplying liquid to the spray tool (100), and only when a preset pressure is reached in the liquid supply pipe the second control valve (107) is opened in order to supply the spray tool (100) with granulate suspended in the propellant and with the said gaseous propellant in addition to the fluid conveyed by the pump.
- A wet spray installation according to claims 8 and 9, characterised in that the necessary operating pressure in the pressure vessel (105) is obtained with only a part of the gaseous propellant.
- A wet spray installation according to claims 8 to 10, characterised in that the ratio between the amount of gaseous propellant supplied to the pressure vessel and the gaseous fluid supplied to the vibrator (117) is determined by a pair of valves (118, 120) disposed downstream in parallel with the additional control valve (107).
- A wet spray installation according to claims 9 to 11, characterised in that the excess gaseous fluid from the pressure container (105) and the exhaust gas from the pump motor (110) are brought together in a heat exchanger (122) before the gas mixture leaves the installation.
- A wet spray installation according to claim 12, characterised in that the gas mixture leaves the installation through a silencer (123) disposed downstream of the heat exchanger (122).
- A wet spray installation according to any of claims 9 to 13, characterised in that the gaseous fluid is provided by a compressor and the liquid is provided from a central network.
- A wet spray installation according to any of claims 9 to 14, characterised in that the dependence of operation of one control valve (106) on the other control valve (107) is effected by means of a pressure-dependent signal transmitter (112) in the supply pipe between the pump (111) and the spray tool (100).
- A wet spray installation according to claim 15, characterised in that the signal transmitter (112) can be automatically overridden in order to supply liquid exclusively independently of pressure to an individual liquid outlet nozzle (102) of the spray tool (100).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19623024 | 1996-06-08 | ||
DE19623024A DE19623024A1 (en) | 1996-06-08 | 1996-06-08 | Wet jet plant |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0832719A2 EP0832719A2 (en) | 1998-04-01 |
EP0832719A3 EP0832719A3 (en) | 1998-11-04 |
EP0832719B1 true EP0832719B1 (en) | 2003-04-16 |
Family
ID=7796477
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP97109332A Expired - Lifetime EP0832719B1 (en) | 1996-06-08 | 1997-06-09 | Wet-blast installation |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP0832719B1 (en) |
AT (1) | ATE237431T1 (en) |
DE (2) | DE19623024A1 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19910563A1 (en) * | 1999-03-10 | 2000-09-14 | Torbo Engineering Keizers Gmbh | Cleaning device and method |
KR20010014577A (en) * | 1999-03-18 | 2001-02-26 | 시부야 히로토시 | Method and apparatus for cleansing and scraping and method and apparatus for forming a cleansing and scraping media flow |
CN108857915B (en) * | 2018-09-29 | 2023-07-18 | 广东水拓工程科技有限公司 | Wet-type sand blasting system |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3858358A (en) * | 1973-01-02 | 1975-01-07 | American Aero Ind | High pressure liquid and abrasive cleaning apparatus |
HU191769B (en) * | 1985-01-29 | 1987-04-28 | Ferenc Hollosi | Grain-spreading apparatus and charging tap belonging to the apparatus of this kind |
DE3643060A1 (en) * | 1986-04-22 | 1987-11-19 | Peiniger Ernst Gmbh | Safety device |
US4821467A (en) * | 1986-06-06 | 1989-04-18 | Whitemetal Inc. | Control system for liquid propelled abrasive cleaning |
US5412910A (en) * | 1987-12-04 | 1995-05-09 | Whitemetal, Inc. | Wet abrasive blasting method and apparatus |
US4901928A (en) * | 1988-10-04 | 1990-02-20 | Stripping Technologies Inc. | Pressure hose handle and system |
WO1994027785A1 (en) * | 1993-05-26 | 1994-12-08 | Carolina Equipment And Supply Company, Inc. | Method and apparatus for cleaning with high pressure liquids at low flow rates |
DE4209353C2 (en) * | 1992-03-23 | 1994-12-15 | Pro Aqua Geraete Gmbh | Wet blasting system with a blasting gun |
DE4244348C2 (en) * | 1992-12-28 | 1996-09-19 | Johann Szuecs | Device for feeding a blasting gun with non-subliming fine or dusty blasting material |
DE29607056U1 (en) * | 1996-04-18 | 1996-07-18 | Gries, Josef, 82008 Unterhaching | Device for supplying a blasting gun with working media |
FR2753643B1 (en) * | 1996-09-24 | 1998-12-04 | DEVICE FOR CONTROLLING A CLEANING INSTALLATION FOR CONTAMINATED SURFACES |
-
1996
- 1996-06-08 DE DE19623024A patent/DE19623024A1/en not_active Withdrawn
-
1997
- 1997-06-09 EP EP97109332A patent/EP0832719B1/en not_active Expired - Lifetime
- 1997-06-09 AT AT97109332T patent/ATE237431T1/en not_active IP Right Cessation
- 1997-06-09 DE DE59709834T patent/DE59709834D1/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
DE19623024A1 (en) | 1997-12-11 |
EP0832719A2 (en) | 1998-04-01 |
DE59709834D1 (en) | 2003-05-22 |
ATE237431T1 (en) | 2003-05-15 |
EP0832719A3 (en) | 1998-11-04 |
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