GB2296556A - Method and apparatus for drying objects (e.g. bearings) - Google Patents

Abstract

A vacuum degreasing-drying method by which extremely small, precision metal products can be degreased and dried quickly and completely without using organic solvents, entails placing an object (112) in a vacuum drier (110) after it has been rinsed with a hydrocarbon cleaning agent in machine 113 and then the air in the vacuum dryer (110) is evacuated so as to degrease and dry the object. The object is passed through a degreasing machine 114 to be degreased by air jetted from nozzles 122. <IMAGE>

Description

METHOD AND APPARATUS FOR DRYING BEARING The present invention relates to a vacuum degreasing-drying method and more particularly to a vacuum degreasing-drying method for degreasing and drying extremely small, precision metal products, especially extra small diameter miniature bearings and their parts after they have been rinsed with a hydrocarbon cleaning agent.

Conventional methods for degreasing and drying extremely small, precision metal products and the like complicated in configuration, after they have been rinsed with a hydrocarbon cleaning agent, generally employ, for instance, chlorine organic solvents such as freon and 1, 1, l-trichloroethane which are highly volatile at normal temperature, alcoholic organic solvents such as ethanol, highly volatile petroleum hydrocarbon such as gasoline and petroleum benzine, and chemical compound organic solvents such as benzine, hexane and toluene after a hydrocarbon rinsing process. Such organic solvents are employed for degreasing and drying to ensure that even extremely small, precision metal products can be degreased and dried quickly. Particularly, the use of freon and 1, 1, l-trichloroethane is effective in degreasing and drying extra-small diameter miniature bearings.

Notwithstanding, the use of such freon, 1, 1, 1-trichloroethane and the like has been restricted because they cause great destruction of the ozone layer. Moreover, low inflammable organic solvents need to satisfy complete explosion-proof specification as they are under rigid restrictions due to the fire laws and the use of them costs a great deal. As a result, a number of problems arise when organic solvents are used because the poisoning preventive regulations are applied to the organic solvents, for instance.

Therefore, efforts may be attempted to degrease and dry extremely small, precision metal products without using the aforementioned organic solvents; however, the problems is that it is still impractical to do so because a great deal of time is consumed for drying and because productivity is considerably reduced. When some of the hydrocarbon cleaning agent is left on the surface of such an extra-small diameter, miniature bearing and its parts as it has been dried incompletely, for instance, the application of grease thereto at the following process step may result in lowering the viscosity of the grease, thus causing grease leakage and the spread of the hydrocarbon cleaning agent.In addition to these problems, the acoustic quality of the bearing may deteriorate or the bearing may fail to come in contact with the shaft of a HDD spindle (hard disk drive spindle) motor or the housing, which may cause dust to gather therein.

An object of the present invention is to solve the foregoing problems by providing a decompression-degrease dying method by which extremely small, precision products are degreased and dried completely and quickly without using the aforementioned organic solvents.

According to the present invention, a vacuum degreasing-drying method comprises the steps of: rinsing an object with an aqueous solvent or a hydrocarbon type solvent cleaning agent; putting the object thus rinsed in a hermetic container; and evacuating the air in said hermetic container loaded with said rinsed object, to reduce the boiling point of the said aqueous solvent or hydrocarbon cleaning agent.

More specifically, the vapour pressure of the hydrocarbon cleaning agent increases when the air in the hermetic container is evacuated and the boiling point of the hydrocarbon cleaning agent sticking to the rinsed object becomes lower than its boiling point at the atmospheric pressure. Consequently, the hydrocarbon cleaning agent becomes easier to vaporize than when it is at atmospheric pressure. The rinsed object can thus be degreased and dried completely and quickly as the degreasing and drying process is considerably accelerated.

Moreover, various problems heretofore originating from the use of organic solvents can thoroughly be solved since no organic solvents are used and cost reduction is made possible by the vacuum degreasing-drying method according to the present invention.

Furthermore, it is also possible to improve degreasing- drying efficiency by heating the object in the hermetic container using such as an infrared heater, a high-frequency heater or the like.

BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is a sectional view of a drying apparatus disclosed in our co-pending application GB-A-2,268,253 from which the present application is divided, and which may be used in conjunction with the present invention; Figures 2(a)-2(d) are sectional views of a workpiece to be dried through the process illustrated according to GB-A-2,268,253, respectively; Figure 3 is a sectional view of a drying apparatus according to a second embodiment disclosed in GB-A2,268,253; Figure 4 is a sectional view of a drying apparatus according to a third embodiment disclosed in GB-A2,268,253; Figure 5 is a sectional view of a drying apparatus according to a fourth embodiment disclosed in GB-A2,268,253; Figure 6 is a water saturation curve; Figure 7 is a vacuum pump performance curve;; Figure 8 is a block diagram illustrating vacuum degreasing-drying process steps according to the present invention; Figure 9 is a graph showing the relation between the atmospheric pressure and the vapour amount at the time hydrocarbon cleaning agents are dried according to the present invention; and, Figure 10 is a graph showing the relation between the atmospheric temperature and the vapour amount at the time hydrocarbon cleaning agents are dried according to the present invention.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Referring to the accompanying drawings, an example of a drying method and apparatus as disclosed in our copending application GB-A-2,268,253 from which the present application is divided, which method and apparatus can be employed in conjunction with the present invention will be described.

As shown in Figure 1, a hermetic container in the apparatus comprises a lower mould 1 and an upper mould 5, an internal space 9 of the lower mould and an internal space 10 of the upper mould constituting an internal space 20 of the hermetic container.

The lower mould 1 has the internal space 9 and a circular work guide 2 is supported by and fixed onto the stepped portion on the inner periphery of the space 9 therein, the circular work guide having a slide guide face capable of loading/unloading workpieces (bearings) when those successively conveyed on a production line are put in the hermetic container. The internal spaces 9, 10 of the lower and upper moulds communicate with each other via the work guide 2, which is slatted so that air can circulate through the internal spaces 9, 10 of the lower and upper moulds. Moreover, a vacuum pump 3 is connected via a solenoid valve 4 to the internal space 9 of the lower mould in order to pump out the air from the internal space 20 of the hermetic container.

On the other hand, the upper mould 5 has the internal space 10 formed in such a way that the workpiece 8 can be hermetically sealed therein and a high-frequency heater 6 for heating the workpiece 8 is installed on the periphery of the ceiling of the internal space 10 of the upper mould.

Further, the upper mould 5 is provided with an O-ring 7 having a sealing effect in insulating the internal space 20 of the hermetic container from the outside when the lower mould 1 is combined with the upper mould 5.

The workpiece for use in the embodiment shown is so constructed that, as shown in Figure 1, balls are held by a plastic retainer between an outer and an inner ring. In the conventional drying method, there develops a shady portion as the contact part between the ball and the retainer is complicated in configuration and this results in requiring a longer time for drying.

Referring to sectional views of a workpiece to be dried, the operation of the drying apparatus will subsequently be described.

At the step of Figure 2(a), the lower mould 1 and the upper mould 5 are in a vertically separated condition in which the loading of each of the workpieces 8 successively conveyed on a production line is waited for. At this time, the solenoid valve 4 is in the state of OFF (in which the piping extended from the vacuum pump 3 remains cut-off) and the power supply of the high-frequency heater 6 is also in the state of OFF.

At the step of Figure 2(b), the workpiece 8 conveyed on the line is subsequently caused to slide on the surface of the work guide 2 and loaded in position.

At the step of Figure 2(c), the upper mould 5 is mounted on the lower mould 1 and these moulds are tightly coupled together by means of an actuator such as a cylinder (not shown). At this time, the internal space 20 of the hermetic container is insulated by the O-ring 7 having the sealing effect from the outside. Then the solenoid valve 4 is turned on (i.e. the piping extended from the vacuum pump 3 is opened) to reduce the pressure in the internal space 20 of the hermetic container to 0.1 - 0.3 atmosphere.

Subsequently, the power supply of the high-frequency heater 6 is turned on to raise the temperature of the workpiece 8 to 50 - 800C for drying purposes. High-frequency heating at this time makes it possible to heat and dry the workpiece 8 uniformly.

At the step of Figure 2(d), the power supply of the high frequency heater 6 is turned off and the solenoid valve 4 is also turned off so as to separate the lower mould 1 from the upper mould 5. As the pressure in the internal space 20 of the hermetic container then sharply rises up to the atmospheric pressure, the workpiece 8 is sufficiently dried further. Subsequently, the workpiece 8 is unloaded and discharged from the work guide 2. The state of Figure 2(a) is then restored.

The next workpiece conveyed on the line is also passed through the same process and those successively conveyed thereon can be dried consecutively.

Figure 3 is a sectional view of a second embodiment of a drying apparatus disclosed in GB-A-2,268,253, wherein the apparatus similar to what is shown in Figure 1 is equipped with a choke device and a filter.

In the drying apparatus of Figure 3, the upper mould 5 of what is shown in Figure 1 is supplied with a choke device 51 communicating with the internal space 10 thereof and the choke device 51 is connected via piping 50 to a filter 52, whereby air can circulate through the internal space 20 of the hermetic container.

Until the lower mould 1 is separated from the upper mould 5 on the termination of reducing the pressure in the internal space 20 of the hermetic container at the step of Figure 2(d) after the reduction of the pressure therein is started at the step of Figure 2(c), the choke device 51 operates to regulate the flow rate of clean air passing through the filter 52 and the air is introduced into the internal space 20 of the hermetic container. Saturated vapour existing in the internal space 20 of the hermetic container is thus expelled to prevent rust from gathering on the workpiece with the effect of brushing it with clean air.

Figure 4 is a sectional view of a third embodiment of a drying apparatus shown in GB-A-2,268,253, wherein instead of the high-frequency heater 6 of the drying apparatus of Figure 1, an infrared heater 53 is employed.

The use of such an infrared heater 53 makes radiation heating possible.

Figure 5 is a sectional view of a fourth embodiment of a drying apparatus shown in GB-A-2,268,253, wherein a piping part, a solenoid valve and an oil mist lubricator are provided for the upper mould of the apparatus similar to what is shown in Figure 1 and wherein an additional solenoid valve is also provided for the lower mould thereof.

The upper mould 5 of the drying apparatus of Figure 5 similar to what is shown in Figure 1 is equipped with a piping part 54 in such a way as to communicate with the internal space 10 of the upper mould and a solenoid valve 55 is connected via piping 50 to the piping part 54.

Further, the solenoid valve 55 is consecutively connected to an oil mist lubricator 56 loaded with rust preventive oil. The rust preventive oil is introduced into the internal space 20 of the hermetic container and made to stick to the workpiece 8 therein. An additional solenoid valve 57 is connected to the lower mould 1, thus allowing air to circulate from the outside to the internal space 20 of the hermetic container.

With respect to the operation of the solenoid valve 55, the oil mist lubricator 56 and the solenoid valve 57, the solenoid valves 55, 57 are held OFF until the steps of Figures 2(a) to 2(c) are taken. The solenoid valve 4 is turned off after the step of Figure 2(c) has been taken and then the solenoid valves 55, 57 are turned on to introduce the rust preventive oil from the oil mist lubricator 56 via the piping part 54 into the internal space 20 of the hermetic container. Part of the rust preventive oil thus introduced sticks to the workpiece 8 and the remainder is discharged from the hermetic container via the solenoid valve 57. The workpiece 8 is thus rendered rust proof through the process mentioned above.

Since a bearing having a plastic portion has been used as a workpiece in this embodiment, the pressure in the internal space of the hermetic container is set at 0.1 0.3 atmosphere and the workpiece is heated up to 50 - 800C in consideration of the allowable plastic heating temperature (about 90CC) at the step of Figure 2(c).

However, the set conditions are not limited to those enumerated above but the pressure therein as well as the work heating temperature may be set in harmony with allowable heating temperatures, depending on the material quality of the workpiece. At this time, the relation between the pressure and the work heating temperature may preferably be determined by saturation curves of Figure 6.

Further, Figure 7 shows a performance curve of the vacuum pump used in this embodiment. As shown in Figure 7, the discharge speed can be held constant (1,500 g/min) even though the pressure in the internal space of the hermetic container is reduced to 0.1 - 0.3 atmosphere. Consequently, this hermetic container is seen to offer a stable pressure reduction performance. Furthermore, the workpiece can be dried more efficiently by determining the pressure in the internal space of the hermetic container and the temperature at which the workpiece is heated in dependence of the performance (capability) of a vacuum pump for use.

It is also possible to promote water evaporation by decreasing the pressure in the internal space of the hermetic container as much as possible within the range of the performance of the vacuum pump. Moreover, the drying period can be made shorter by raising the temperature as much as possible at which the workpiece is heated within the allowable heating range.

Although the workpiece has been heated after the pressure in the internal space of the hermetic container is decreased to prevent the workpiece from gathering rust at the step of Figure 2(c), the reduction in pressure may be made simultaneously with heating when a workpiece is made of rust proof material. The drying cycle time is also reducible by making the pressure reduction and the heating simultaneously.

The internal space of the hermetic container should preferably be formed as narrow as possible within the range allowed to seal the workpiece. The narrower the internal space of the hermetic container, the greater the pressure reduction effect improves, whereby the workpiece can be dried efficiently in a short time.

Although the high-frequency heater has been installed in the internal space of the upper mould in the drying apparatus shown in Figure 1, it may otherwise be positioned anywhere on condition that the workpiece can be heated.

Moreover, the vacuum pump and the solenoid may also be positioned anywhere on condition that the pressure in the internal space of the hermetic container is reducible.

Although the choke device 51 and the filter 52 have been so arranged as to communicate with the internal space 10 of the upper mould in the drying apparatus shown in Figure 3, they may otherwise be positioned anywhere on condition that clean air passing through the filter 52 can be introduced into the internal space of the hermetic container.

Although the piping part 54, the solenoid valve 55 and the oil mist lubricator 56 have been so arranged as to communicate with the internal space of the upper mould and the solenoid valve 57 to communicate with the internal space of the lower mould in the drying apparatus shown in Figure 5, they may otherwise be positioned anywhere on condition that rust preventive oil can be introduced into the internal space of the hermetic container and discharged from the drying apparatus.

Moreover, though a description has been given of the drying apparatus which is divided into the upper and lower moulds, it may otherwise be divided bi-symmetrically, diagonally or into more than two parts.

Further, the means of heating the workpiece may optionally be selected from among a high-frequency heater, an infra-red heater, a Nichrome wire, a ceramic heater and the like.

Although one workpiece has been dried each time in the embodiment shown, a plurality of workpieces, if desired, may be dried at a time.

Figure 8 is a block diagram illustrating a vacuum degreasing-drying process according to the present invention.

In the vacuum degreasing-drying process shown in Figure 8, use may be made of a parts feeder 111 for feeding objects 112 to be rinsed, a rinsing machine 113 using a hydrocarbon for rinsing the object 112 fed from the parts feeder 111, a degreasing machine 114 for degreasing the object 112 by air after the hydrocarbon-rinsing operation has been done, a product can 115 for accommodating the objects thus degreased by air, the product can 115 being provided with a net cage or a finger shelf for flatly putting the objects 112 side by side, and a vacuum drier 110 for vacuum-drying the objects 112 thus accommodated in the product can 115.

The parts feeder 111 and the rinsing machine 113 are continuously coupled together via a belt conveyor 128 and the object 112 to be rinsed is conveyed by the belt conveyor 128 from the parts feeder 111 to the rinsing machine 113.

The rinsing machine 113 has an open entrance 124, an open exit 125 and nozzles 121 for sending out a jet of cleaning agent to the object 112, the nozzles being located above and between the entrance 124 and the exit 125.

Further, a rinsing conveyer 120 for conveying the objects 112 is installed opposite to and under the nozzles 121 in such a way as to pass through the entrance 124 and the exit 125 of the rinsing machine 113. While being conveyed by the conveyer 120 from the entrance 124 to the exit 125 through the rinsing machine 113, the object 112 is rinsed with the cleaning agent jetted from the nozzles 121.

The degreasing machine 114 has an open entrance 126, an open exit 127 and air nozzles 122 for sending out air to the object 112, the air nozzles being located above and between the entrance 126 and the exit 127. Further, a degreasing conveyor 129 for conveying the objects 112 is installed opposite to and under the air nozzles 122 in such a way as to pass through the entrance 126 and the exit 127 of the degreasing machine 114. While being conveyed by the conveyer 129 from the entrance 126 to the exit 127 through the degreasing machine 114, the object is degreased by the air jetted from the nozzles 122.

An orientation means 130 arranges flatly the objects 112 discharged from the degreasing machine 114 in the product can 115.

The vacuum drier 110 comprises a spare chamber 116 and a vacuum chamber 117 with a partition 123 for separating the former from the latter, and a drier entrance 131 that can be opened and shut is provided on the spare chamber side 116. When the entrance 131 of the drier is shut, the spare chamber 116 can be held in a hermetic condition and the partition 123 is shut for evacuating the air or for hot air drying, so that the remaining cleaning agent sticking to the object 112 being rinsed is preliminarily dried. The object 112 being rinsed is preliminarily dried to ensure that full drying time in the vacuum chamber -117 can be shortened. An open/close gateway 132 for the object is installed, whereby the object 112 to be dried can be reciprocated between the spare chamber 116 and the vacuum chamber 117.When the gate way 132 is closed, the vacuum chamber 117 can be held in a hermetic condition. A vacuum pump 119 for evacuating the air in the vacuum chamber 117 is coupled to the vacuum chamber 117 and further an infrared heater 118 for heating the object 112 is also installed.

The product can 115 and the vacuum drier 110 may be connected via a belt conveyer (not shown), for instance, by which the product can 115 accommodating the objects 112 to be rinsed can be conveyed up to the vacuum drier 110.

Otherwise, the vacuum drier 110 may be installed independently and conveyed up to the vacuum drier 110 by a conveying means such as a dolly.

In this embodiment, the vacuum drier 110 is provided with the infrared heater 118 for heating the object 112.

However, not only the infrared heater but also any other heating means such as a high-frequency heater, a ceramic heater and an electric heater may be installed. Moreover, the installation of the heating means is not necessarily essential.

Although the vacuum drier 110 has been divided into the spare chamber 116 and the vacuum chamber 117 in this embodiment, it is unnecessary to do so as long as the vacuum drier 110 can be hermetically sealed to create a vacuum and the vacuum drier may be formed into one room.

Moreover, the parts feeder 111, the rinsing machine 113 and the air degreasing machine 114 have been described only by way of example in this embodiment. However, any other known apparatus of that sort may be employed or what has other additional functions may needless to say be installed when desired.

Referring to Figure 8, the vacuum drier 110 has been described in this embodiment. Alternatively, the drying means may be as shown in GB-A-2,268,253 and -as hereinbefore described with respect to Figures 1 to 7. More specifically, the method therefor comprises the steps of forming a hermetic container by combining a plurality of divided moulds together and conveying bearings successively into the hermetic container, evacuating the air in the hermetic container, and heat-drying the bearing. With this method and apparatus, the object of the present invention is also accomplishable.

In a method according to the present invention, the object 112 is first supplied from the parts feeder 111, is conveyed by the belt conveyer 128 up to the rinsing machine 113, put by the rinsing conveyer 120 in the rinsing machine 113 through its entrance 124, and made to proceed in the rinsing machine 113 toward the exit 125. During this time, the object is rinsed with jets of the hydrocarbon cleaning agent from the nozzles 121. Incidentally, illuminating kerosine was used as the hydrocarbon cleaning agent in this embodiment.

The object 112 discharged from the exit 125 of the rinsing machine is subsequently conveyed from the rinsing conveyer 120 to the degreasing conveyer 129 before being conveyed to the degreasing machine 114. The object 112 thus conveyed to the degreasing machine 114 put by the degreasing conveyer 129 in the degreasing machine 114 through the entrance 126 and caused to proceed in the degreasing machine 114 toward the exit 127. During this time, the object 112 is degreased by the air blow jetted from the air nozzles 122. Although the method of degreasing the cleaning agent sticking to the object 112 by the air blow has been described in this embodiment, the object 112 may be put in a container capable of flingering (e.g., a net cage or the like) and subjected to centrifugal degreasing (e.g., 3,200 r.p.m).The object 112 thus degreased may be conveyed to the space chamber 116 of the vacuum drier 110 for the purpose of preliminary drying by using the container as the product can 115.

Thus object 112 discharged from the degreasing machine 114 is conveyed from the degreasing conveyer 129 to the orientation means 130 by which it is accommodated in the product can 115.

The product can 115 accommodating the objects 112 is conveyed to the vacuum drier 110 and put in the spare chamber 116 through the entrance 131 of the drying machine.

Subsequently, the entrance 131 is closed so as to carry out preliminary drying in the hermetic spare chamber 116. The preliminary drying may, as set forth above, be carried out while another object 112 is being subjected to thorough vacuum drying in the vacuum chamber 117 by shutting the partition 123. Then the gateway 132 for the object is opened and the product can 115 in the spare chamber 116 is transferred to the vacuum chamber 117 and then the gateway 132 therefor is closed. Subsequently, the vacuum pump 119 is first operated so as to create a vacuum in the vacuum chamber 117 and the object 112 being rinsed is heated by the infrared heater 118 up to about 800C. At this time, the pressure in the vacuum chamber 117 was reduced up to 760 x 103 - 760 x 10 Torr (10 3 - 10 atmosphere).

The object 112 thus rinsed was completely dried quickly in this way.

Although illuminating kerosine was used as the hydrocarbon cleaning agent in this embodiment, not only illuminating kerosine but also a cleaning agent such as 'Actrel' 1178L, 1140L, llllL of Exson chemical having physical and chemical properties equivalent to those of illuminating kerosine obtained by distilling petroleum, or petroleum or hydrocarbon light oil may be selected as occasion demands.

The pressure in the vacuum chamber 117 has been reduced up to 760 x 10-3 760 x 10 Torr in this embodiment. However, not only this decompressed condition but also 10 Torr or an atmospheric pressure of 0.1 - 0.3 may properly be selected, depending on the object 112 being rinsed or the cleaning agent.

Further, the relation between the atmospheric pressure and the vapour amount at the time the hydrocarbon cleaning agent is dried (vaporized) was examined in the following method.

The aforementioned rinsing machine 113 was used to rinse miniature bearings (#695) as finished objects to be rinsed, which were degreased by means of the degreasing machine 114. At this point of time, 5 mg of hydrocarbon cleaning agent was seen to stick to each bearing thus air-degreased. Subsequently, the dry conditions of the bearings were observed in both cases where the vacuum chamber was set at 10 Torr, 25"C and at the atmospheric, 250C, using the vacuum drier 110. With respect to hydro carbon cleaning agents, commercial products (petroleum hydrocarbon of C8 - C12) obtained by distilling illuminating kerosine and kerosine) were used. Figure 9 shows the test results.

As shown in Figure 9, it was confirmed that drying time was conspicuously shortened when the air in the vacuum chamber 17 was evacuated (10 Torr, 25CC) as compared with a case where it was not evacuated (atmospheric pressure).

Subsequently, the relation between the atmospheric temperature and the vapour amount at the time the hydrocarbon cleaning agent was dried (vaporized) was examined in the following method.

As samples of hydrocarbon cleaning agents, 20 ml of illuminating kerosine was put on three laboratory dishes and these samples were placed in constant temperature baths respectively at 250C, 600C and 800C (at the atmospheric pressure) and the remaining amount of the illuminating kerosine thus evaporated was observed. Figure 10 shows the test results.

As shown in Figure 10, it was confirmed that the sample in the constant temperature bath at 800C was completely vaporized for about 90 minutes; the sample in the constant temperature bath at 600C was completely vaporized for about 135 minutes; however, over 60% of the sample in the constant temperature bath at 250C was seen to remain after elapse of more than 6 hours. As is obvious from the test results, the evaporation of the hydrocarbon cleaning agent was undoubtedly accelerated when the atmospheric temperature and the degree of vacuum were increased.

As set forth above, the evaporation of the hydrocarbon cleaning agent sticking to the object to be rinsed can be accelerated by evacuating the air in the hermetic container in which the object rinsed with the hydrocarbon cleaning agent is put in the vacuum degreasing-drying method according to the present invention. Therefore, the object to be rinsed which is not only complicated in configuration but also small in size can be degreased and dried quickly and completely without using organic solvents. As a result, various problems heretofore originating from the use of organic solvents can thoroughly be solved and cost reduction is also made possible.

Claims (6)

1. A vacuum degreasing-drying method comprising the steps of: rinsing an object with an aqueous solvent or a hydrocarbon type solvent cleaning agent; putting the object thus rinsed in a hermetic container; and evacuating the air in said hermetic container loaded with said rinsed object, to reduce the boiling point of the said aqueous solvent or hydrocarbon cleaning agent.

2. A vacuum degreasing-drying method according to claim 1, further comprising the steps of: degreasing the solvent sticking to said object, said degreasing step being conducted after rinsing the object and before putting the object in the hermetic container.

3. A vacuum degreasing-drying method according to claim 2, in which said degreasing step is operated in such a manner that said object is degreased an air jet from a degreasing machine or by centrifugal degreasing.

4. A vacuum degreasing-drying method according to any one of the preceding claims, further comprising the steps of: heating said object in said hermetic container after evacuating.

5. A vacuum degreasing-drying method according to claim 4, in which said object is heated up to about 800C in the heating step.

6. A vacuum degreasing-drying method according to any one of the preceding claims, in which said rinsing step is operated in such a manner that said object is rinsed with jets of said hydrocarbon cleaning agent.

6. A vacuum degreasing-drying method according to any one of the preceding claims, in which said rinsing step is operated in such a manner that said object is rinsed with jets of said hydrocarbon cleaning agent.

7. A vacuum degreasing-drying method according to any one of the preceding claims, in which the pressure in an internal space of the hermetic container is reduced up to 10 - 10 atmosphere in said air evacuating step.

8. A method substantially as described with reference to Figures 8 to 10.

9. An apparatus substantially as described with reference to Figures 8 to 10.

Amendments to the claims have been filed as follows 1. A vacuum degreasing-drying method comprising the steps of: rinsing an object with a hydrocarbon type solvent cleaning agent; putting the object thus rinsed in a hermetic container; and evacuating the air in said hermetic container loaded with said rinsed object, to reduce the boiling point of the said hydrocarbon cleaning agent.

2. A vacuum degreasing-drying method according to claim 1, further comprising the steps of: degreasing the solvent sticking to said object, said degreasing step being conducted after rinsing the object and before putting the object in the hermetic container.

3. A vacuum degreasing-drying method according to claim 2, in which said degreasing step is operated in such a manner that said object is degreased an air jet from a degreasing machine or by centrifugal degreasing.

4. A vacuum degreasing-drying method according to any one of the preceding claims, further comprising the steps of: heating said object in said hermetic container after evacuating.

5. A vacuum degreasing-drying method according to claim 4, in which said object is heated up to about 800C in the heating step.