the existing sterilizing systems using liquid hydrogen peroxide as sterilant , such as those described in the u . s . patents cited above , are very effective . however , a stabilizer is usually added to the hydrogen peroxide during its storage to stabilize the hydrogen peroxide , and most such stabilizers are in solid state . when used , the solid stabilizers is dissolved in hydrogen peroxide , and the liquid hydrogen peroxide with dissolved stabilizer is injected into a sterilizing chamber where the liquid hydrogen peroxide or its solution is vaporized under vacuum and / or elevated temperature . during this vaporizing process , the dissolved solid stabilizer separates from the liquid phase and forms tiny particulates traveling with the vapor stream and with any incompletely vaporized liquid droplets generated from the injected liquid hydrogen peroxide , and deposits on the surfaces of articles to be sterilized in the sterilizing chamber . the deposition of the solid stabilizer residue on the article surface is very undesirable , because it presents an unsightly product image to hospital personnel . referring to fig1 there is schematically illustrated a cylindrical chamber 10 having a door 12 on one end . the chamber is connected to a suitable vacuum source by way of a conduit 14 . the chamber is adapted to receive items to be sterilized , such as surgical instruments , in accordance with a method outlined in u . s . pat . no . 4 , 643 , 876 which is incorporated herewith by reference , wherein a liquid such as hydrogen peroxide is introduced into the chamber . for delivering such fluid , in accordance with the present invention , there is provided a fluid injection system 16 positioned adjacent to the chamber 10 . the system includes a cassette or cartridge 18 containing the fluid to be injected , a cassette receiving , positioning and clamping mechanism 20 , and a fluid injector valve assembly 22 mounted on and interconnected with the chamber . an injector impinger 200 ( not shown ) is secured to the fluid injector valve assembly 22 or to other part of the chamber . the fluid injector system 16 can be thought of as a pump in which the cassette 18 is inserted into the cassette receiving mechanism 20 and doses of the media contained in the cassette are automatically injected into the chamber during automated sterilizing cycles . the system described above is similar to the system disclosed in u . s . 4 , 938 , 262 which is incorporated herewith by reference , except for the addition of an injector impinger . the significant advantage of the system of the present invention results from the addition of the injector impinger 200 inside the chamber . for example , the injector impinger can be positioned at the vapor outlet of the fluid injector valve assembly 22 with or without modifications to the structure of the fluid injector valve assembly 22 . other modifications on the system of u . s . pat . no . 4 , 938 , 262 , in addition to the introduction of an injector impinger , are made in the present invention . thus , in one preferred embodiment of the present invention , the fluid injector valve assembly 22 is replaced by an injection assembly 22b as shown in fig2 . the sterilizing chamber of the present invention may also further include an electrode for generating plasma , and has a rectangular cross - sectional area or any other appropriate shape . in one preferred embodiment , the injection assembly 22b is mounted and sealed to the chamber 10 . the injection assembly 22b can be further provided with a pressure relief valve connecting to a liquid injection device . as shown in fig2 the injection assembly 22b has an body 100 which is mounted and sealed to the chamber 10 . a valve outlet passage 102 for receiving liquid hydrogen peroxide or other fluid from a liquid injection device such as that shown in fig1 . an 0 - ring seal 104 is provided to secure the sealing around the valve outlet passage 102 . the valve outlet passage intrudes into a vaporizer bowl 106 where the injected liquid is vaporized . the vaporizer bowl is defined by the body 100 and a second piece 108 . the valve outlet passage 102 is also located at the center of the second piece 108 . vapor passage 110 is provided to connect the vaporizer bowl 106 to the chamber 10 . vapor generated from the injected liquid in the vaporizer bowl 106 travels through the vapor passage 110 from the vaporizer bowl 106 to the chamber 10 and forms a vapor stream or vapor jet together with solid stabilizer residue particulates and entrained liquid droplets . at the bottom portion of the body 100 , there is an extrusion part with a male thread 112 for receiving the injector impinger . the injection assembly is also equipped with a heating device ( not shown ) for keeping a desired temperature at the vaporizer bowl 106 and the valve outlet passage 102 . the operation temperature may vary , preferably in a range of about 20 - 80 , more preferably about 55 - 65 ° c . an injector impinger 200 is attached to the injection assembly as shown in fig2 . referring to fig3 and 4 , the injector impinger has a conically - shaped central section 202 , a flat disk section 204 surrounding the conically - shaped section 202 , and a downward extrusion piece 205 in the center with an elongated hole 206 and a female thread 208 on the inner wall of the elongated hole 206 . the injector impinger 200 is secured to the body 100 through the male thread 112 of the body 100 and the female thread 208 of the injector impinger 200 . if desirable , the injector impinger can be provided with a temperature control mechanism to control its temperature . for example , the injector impinger can be made hollow , and cooling or warming fluids are filled into or circulated through the hollow body of the injector impinger . the vapor stream together with the solid stabilizer residue particulates and entrained liquid droplets enters the chamber 10 through the vapor passage 110 , forming a vapor stream or vapor jet . the vapor jet travels at a velocity determined by several factors including the dimension of the vapor passage 110 , the pressure drop between the vaporizer bowl 106 and the chamber 10 , and the temperature of the vapor jet . the vapor jet velocity will change as the vapor jet travels away from the outlet of the vapor passage . although the present invention is not limited to any theory , it is believed that the particulate removing mechanism of the present invention is based on fluid dynamic principles . thus , when the vapor jet is entering the chamber 10 from the outlet of the vapor passage , the vapor entrained liquid droplets and the tiny particulates travel along straight stream lines at certain velocity . once the vapor jet is disturbed by an object , the stream line 210 of the vapor jet will change direction as shown in fig3 according to the shape of the surface of the object . because of their mass , the particulates and entrained liquid droplets can no longer follow the stream line 210 . instead , the particulates and entrained liquid droplets will travel along a path 212 between the straight stream line and the changed curved stream line 210 , and impinge the surface of the injector impinger 200 . the particulates will stick to the surface of the injector impinger . apparently , velocity of the vapor jet is an important factor affecting particulate removing efficiency . thus , the distance between the particulate - collecting surface of the injector impinger and the outlet of the vapor passage will affect particulate - removing efficiency . the shape of the particulate - collecting surface and the angle between the stream line and the surface also have important effects . preferably , the particulate - collecting surface is positioned perpendicular to the stream line . other options are obvious based on the teaching of the present invention . for example , the injector impinger does not have to be a single piece , does not have to be mounted to the injection assembly 22b , and does not have to be the shape as described earlier . the vapor passage 110 does not have to be vertical . in stead , it can be directed to the side wall of the chamber 10 , and the particulates are collected in an injector impinger accordingly positioned . the injector impinger can be made of any metal , ceramic , and plastic materials . however , if the injector impinger is used with plasma , it should be made of plasma - compatible materials such as plastics . in a preferred embodiment of the present invention , the injector impinger is made of polypropylene . in the use of the system of the present invention , vacuum is applied to the chamber 10 by way of the conduit 14 . and the pressure in the chamber 10 and the vaporizer bowl 106 is preferably kept below about 1 torr , more preferably between about 0 - 400 mtorr before the liquid agent is injected . then , a liquid agent such as hydrogen peroxide with dissolved solid stabilizer such as fmc is injected into the vaporizer bowl through valve outlet passage 102 . the liquid injection assembly described in u . s . pat . no . 4 , 913 , 196 can be used to make the injection . in order to facilitate the evaporation of the liquid agent , vaporizer bowl 106 of the injection assembly 22b can be heated to a desired temperature , preferably 20 - 80 ° c ., more preferably 50 - 70 ° c . in one preferred embodiment , the vaporizer bowl is heated to 60 ° c . the generated vapor stream flows from the vaporized bowl to the chamber 10 through vapor passage 110 under a pressure drop between the vaporizer bowl 106 and the chamber 10 . the pressure drop is caused by the rapid evaporation of the liquid agent . the vapor stream with solid stabilizer particulates and entrained liquid droplets impinges the upper surface of the injector impinger 200 . a significant percentage of the particulates will be separated from the vapor stream and collected on the surface . as the vapor stream continue to travel along a stream line affected or confined by the injector impinger , a portion of the particulates also continue to follow the vapor stream . in the preferred embodiment shown in fig2 the stream line of the vapor stream will follow the wall of the chamber 10 after impinging the injector impinger 200 . thus , the remaining solid stabilizer particulates will deposit on the walls and bottom of the chamber . after certain cycles of sterilizing operation , the injector impinger can be easily replaced and cleaned . the walls and the bottom of the chamber 10 are also easy to clean . therefore , the particulate deposition on surfaces of the items to be sterilized is eliminated or at least significantly reduced . while the invention for removing particulates from a fluid has been described in connection with injecting liquid into a chamber for a sterilizing cycle , it should be understood that the system is also useful for removing particulates from a liquid to be injected in a process other than sterilization . also , the system can be used to remove particulates from a gas or mist injected into containers other than vacuumized chambers . various modifications can be made without departing from the spirit and scope of the present invention .
a sterilizing system for receiving a stream of solid - stabilizer - containing fluid and sterilizing an article comprises a chamber for receiving the article and an injection assembly coupled to the chamber for generating and introducing a fluid jet into the chamber . the system particularly comprises an injector impinger for removing particulates and liquid droplets from the solid - stabilizer - containing fluid by causing a sudden change of the stream line direction of the fluid jet . the injector impinger is positioned between the injection assembly and the article , so that the fluid jet can not reach the article without first interacting with the injector impinger . a method for removing particulates from a solid - stabilizer - containing fluid in a sterilizing process comprises the steps of providing the fluid , vaporizing the fluid , forming a vapor stream from the vaporized fluid , and removing the particulates and the droplets from the vapor stream by causing a sudden change of direction of stream line of the vapor stream .