the following description sets forth certain illustrative examples of the claimed subject matter . other examples , features , aspects , embodiments , and advantages of the technology should become apparent to those skilled in the art from the following description . accordingly , the drawings and descriptions should be regarded as illustrative in nature . fig1 reflects a sterilization system 10 , depicted schematically in block diagram - format . it comprises , a vacuum chamber 12 having a load ( pack ) 14 of instruments therein to be sterilized . the chamber 12 may be formed of any material that is sufficiently robust to handle pressures as low as approximately between 0 . 15 torr and 3 torr , and sufficiently inert to avoid reacting with or absorbing any sterilants introduced therein . such materials may include aluminum and stainless steel . chamber 12 may also include an openable and sealable barrier 16 , such as a door , that may be opened to allow placement and removal of load 14 into chamber 12 . the barrier should be sufficiently robust , and include a sufficiently robust seal , to withstand low pressures drawn within chamber 12 and avoid leaks between chamber 12 and the ambient environment . a vacuum pump 18 capable of reaching the desired operating pressure evacuates air and other gases , such as water vapor , from chamber 12 . vacuum pump 18 may include a hose or pipe 20 to connect it to chamber 12 . vacuum pump 18 may also include a valve 22 , which may be opened or closed to assist or prevent pressure changes in chamber 12 . for example , when the valve is open and the vacuum pump is operational , the pressure in chamber 12 may be lowered . alternatively , when the valve is open and the vacuum pump is not operational , the pressure in the chamber may be equalized to the ambient pressure . in other embodiments , a venting valve may be used to vent or evacuate chamber 12 to introduce ambient air into chamber 12 and return the pressure within chamber 12 to the ambient pressure . this venting valve , which is not shown in fig1 , may be used instead of or in addition to pump 18 and valve 22 to adjust the pressure within chamber 12 . a hose or pipe may connect chamber 12 to the ambient environment and the venting valve may be disposed within this hose or pipe between the ambient environment and chamber 12 . a pressure monitor 24 monitors the pressure in chamber 12 . particularly suitable pressure monitors are capacitance manometers available from mks instruments . a heating element 26 may be used to heat the chamber 12 . it may comprise separate elements bonded to the outside of the chamber 12 in locations sufficient to uniformly heat the chamber 12 . a tank or reservoir 28 containing sterilant , which includes a hose or pipe 30 , is connected to chamber 12 . in some embodiments , tank 28 may further include a valve 32 , which may be disposed between chamber 12 and tank 28 to control the flow of sterilant from tank 28 through hose 30 and into chamber 12 . in some embodiments , in lieu of or in addition to valve 32 , a seal may be disposed between tank 28 and hose or pipe 30 . the seal may be opened , e . g ., by puncturing , to permit the sterilant enter hose or pipe 30 . accordingly , the seal may be fabricated from , among other things , a sheet of metal or plastic , such as aluminum foil . alternatively or additionally , another hose or pipe with a valve positioned therein may be disposed between tank 28 and the ambient environment to further aid in venting chamber 12 after sterilant has been introduced therein . a power source and / or signal generator 33 and an electrode 34 disposed within chamber 12 may be provided to create an electric field within chamber 12 between electrode 34 and the interior surface of chamber 12 to create a plasma therein . a signal , such as an rf signal , may be provided to electrode 34 from generator 33 by way of a feed through 35 , such as a wire - type feed through . creation of a plasma is useful for low temperature sterilization processes that use hydrogen peroxide gas . in these processes , the hydrogen peroxide gas may be excited to form a hydrogen peroxide plasma . alternatively , another gas may be used to form the plasma , such as air , which may help lower hydrogen peroxide residuals upon the load to facilitate removal of hydrogen peroxide from chamber 12 . sterilization system 10 may also include a user interface 36 , that may include output devices , such as a printer or display , and user - input devices , such as a keypad or touch screen . sterilization system 10 may also include a humidity or relative humidity sensor 50 , such as the hih - 4602 - a / c series relative humidity sensor produced by honeywell international , inc . in some embodiments , a valve 52 is disposed between humidity sensor 50 and vacuum chamber 12 to shield sensor 50 from high concentrations of hydrogen peroxide , which could damage sensor 50 . that is , valve 52 may be in an open state when hydrogen peroxide is not within chamber 12 , thereby allowing sensor 50 to acquire humidity measurements of the air and / or gases within chamber 12 . valve 52 may be in a closed state when hydrogen peroxide is within chamber 12 and / or before hydrogen peroxide is introduced into chamber 12 from sterilant reservoir 28 . when valve 52 is in a closed state , sensor 50 is sealed off from chamber 12 and any hydrogen peroxide therein , thereby protecting sensor 50 from being damaged by hydrogen peroxide . a control system 38 , such as a digital computer , controls the operation of the system 10 and its various components . control system 38 may employ one or more microprocessors 40 . it may also employ a non - transitory storage medium 42 , such as random access memory ( ram ), a hard - disk drive , or flash memory , which can store data , such as pressure values , humidity values , and time values . an analog to digital ( a2d ) converter 44 may be used to convert analog data to digital data if analog data , such as pressure data and / or humidity data , is collected . a timer or clock circuit 45 keeps time . control system 38 may further include software and / or logic by which the microprocessor may determine maximum or minimum values from among the pressure data and / or humidity data . control system 38 may further include software and / or logic by which the microprocessor may compare pressure and / or relative humidity values to other pressure and / or relative humidity values . for example , the control system is capable of storing pressure data p i and humidity data , h i which are acquired at various time increments i . the amount of time between neighboring time increments , designated δt , may be equal to approximately 0 . 1 second , approximately 1 second , approximately 2 seconds , approximately 5 seconds , or approximately 10 seconds . the pressure data and relative humidity data may be measured throughout the sterilization process and stored in storage medium 42 . the data may be collected as voltage outputs from the corresponding pressure or relative humidity sensor . ideally , load 14 is introduced into chamber 12 completely dry , i . e ., without any moisture thereon . in some instances , particularly where the instruments to be sterilized are not sufficiently dried by healthcare personnel , residual water may be introduced into the vacuum chamber . in these instances , water may be in chamber 12 when the vacuum draw of the sterilization process commences , i . e ., when vacuum pump 18 is activated . as the pressure in the chamber decreases , at least a partial volume of the residual water may change phase to gas , which may interfere with a sterilization process , such as a hydrogen peroxide sterilization process . further , at least a partial volume of any residual water that does to change phase to gas may change phase to ice . hydrogen peroxide may condense on this ice and prevent hydrogen peroxide from contacting the device underneath the ice , thereby further decreasing the efficacy of the sterilization process . although the prior art includes examples of identifying moisture in a vacuum chamber via pressure measurements and basing a determination of whether to proceed with a hydrogen peroxide sterilization process based on an analysis of these measurements , the inventors are unaware of any such determinations being based upon an analysis of humidity or relative humidity measurements . previously , humidity - based determinations were believed to be inadequate because of the difficulty humidity and / or relative humidity sensors have detecting water - vapor molecules in vacuum chambers at low pressures appropriate for hydrogen peroxide sterilization . that is , when pressure within a vacuum chamber is lowered from , e . g ., approximately atmospheric pressure to a pressure of , e . g ., approximately 10 torr , the water - vapor molecules that remain in the chamber or that are generated via vaporization do not contact the humidity senor sufficiently to generate an output from the sensor that accurately represents the moisture content in chamber 12 . accordingly , it has been believed that humidity data should not be used to assess moisture content within a vacuum chamber as a basis for a determination of whether to introduce hydrogen peroxide therein . the inventors have discovered a surprising mechanism by which a humidity or relative humidity sensor may be used to measure moisture content within a vacuum chamber such that the measurements may form a basis for determining whether hydrogen peroxide should be introduced into the chamber for the purpose of sterilization . set forth herein is a new , useful , and inventive application of this discovery , which improves sterilization processes and load - conditioning techniques known in the art . in some embodiments , the starting pressure in chamber 12 is equal to or approximately equal to the ambient pressure , e . g ., atmospheric pressure . chamber 12 may be sealed by closing barrier 16 . humidity or relative humidity sensor 50 is used to take a baseline reading of the humidity within chamber 12 . then , air may be withdrawn from chamber 12 by opening valve 22 of vacuum pump 18 and activating the pump to lower the pressure in chamber 12 to a conditioning pressure , p c , of between approximately 5 to approximately 15 torr , approximately 8 torr to approximately 12 torr , or approximately 10 torr . valve 22 may then be closed and pump 18 deactivated in order to maintain the pressure within chamber 12 at p c or approximately p c for a period of time to allow residual water in load 14 to vaporize . vaporization may be assisted by activating heating elements 26 . the period of time , or dwell time , t d , during which valve 22 is closed to maintain pressure may be between approximately 1 second to approximately 5 minutes , approximately 1 second to approximately 1 minute , approximately 1 second to approximately 50 seconds , approximately 1 second to approximately 10 seconds , or approximately 5 seconds . time may be monitored by timer 45 and each time increment δt corresponding to each humidity measurement stored in non - transitory storage medium 42 . correspondingly , throughout the process or a portion thereof , humidity or relative humidity sensor 50 measures the humidity at each time increment δt , and the output of sensor 50 , typically a voltage output , is also recorded in nontransitory storage medium 42 . after the dwell time has passed , chamber 12 is pressurized . for example , valve 22 and / or the venting valve may be opened to allow ambient air into chamber 12 . as air enters or rushes into chamber 12 air and water vapor in the chamber mix and , as the inventors discovered , this activity brings water molecules within chamber 12 into contact with the humidity sensor . if any residual water was introduced into vacuum chamber 12 when load 14 was disposed therein , introduction of air having the same moisture content as the air that was drawn out of chamber 12 causes the overall moisture content within chamber 12 to be greater than what it was originally . that is , the moisture content within chamber 12 should be higher than the baseline moisture content as determined by humidity sensor 50 . for example , in one embodiment , the process begins with ambient air in chamber 12 . hospital personnel dispose load 14 therein , but with a volume of residual water within the load because the load was not sufficiently dried . the pressure in chamber 12 is lowered to a conditioning pressure of approximately 10 torr , valve 22 is then closed , and the pressure maintained at approximately at the conditioning pressure for a dwell time of approximately 0 . 1 seconds , 1 second , 5 seconds , or 10 seconds . from approximately the time at which the pressure in chamber 12 started being lowered , at least some of the molecules of the residual water vaporize . valve 22 or the venting valve is then opened to pressurize and / or vent chamber 12 . this causes , e . g ., ambient air to mix with the air inside the chamber , which has a higher water - vapor content than the ambient air because some of the residual water on load 14 should have vaporized . this mixing mechanism equalizes the vapor - content throughout chamber 12 and allows humidity sensor 50 to “ see ” the water molecules that were vaporized from the residual water . accordingly , despite the notion among those skilled in the art that humidity sensors and humidity data derived therefrom do not enable accurate determinations of whether hydrogen peroxide should be introduced into a chamber or whether a load - conditioning process should be attempted , it appears humidity sensors and humidity data derived therefrom are quite useful in this regard . experiments were performed demonstrating that changes in the moisture content within a vacuum chamber caused by residual water on sterilization loads may be detected using a relative humidity sensor . the experiments were performed using a modified sterrad ® 100nx ® sterilization system , with an hih - 4602 - a / c series relative humidity sensor produced by honeywell international , inc . configured to read humidity within the 100nx &# 39 ; s vacuum chamber . an isolation valve was disposed between the humidity sensor and the vacuum chamber to protect the humidity sensor from potential exposure to hydrogen peroxide . humidity data from one experiment are reflected in the graph of fig2 . the sterilization system used for this experiment was a 100nx ® modified to include a humidity sensor capable or measuring humidity within the vacuum chamber . an isolation valve was placed between the humidity sensor and the vacuum chamber that could be closed to protect the sensor from any hydrogen peroxide that may be introduced into the vacuum chamber . the graph plots voltage output from the humidity sensor versus time . this experiment included two runs . in one run , a wet load containing approximately 5 ml of residual water was disposed in the vacuum chamber . in another run , a dry load was disposed in the vacuum chamber . reference numeral 62 corresponds to the plot of humidity data for the wet load . reference numeral 60 corresponds to the plot of humidity data for the dry load . at t = 0 , while the pressure within the vacuum chamber was the ambient pressure and the ambient temperature was 18 ° c ., the humidity was slightly higher for the wet load . that is , the humidity sensor output a voltage of approximately 1 . 6 volts for the wet load and approximately 1 . 5 volts for the dry load . beginning at approximately t = 0 . 15 minutes , the vacuum pump of the modified 100nx ® began to purge air from the chamber . a notable drop in voltage output from the humidity sensor was observed , which is reflected from approximately t = 0 . 15 minutes ( corresponding to approximately ambient pressure ) to approximately t = 0 . 7 minutes ( corresponding to approximately the conditioning pressure of 10 torr ). during this period , the difference between the two plots of data disappears and the two plots overlap with each other beginning at approximately t = 0 . 4 minutes . this overlap shows that data from the humidity sensor for wet loads and dry loads at lower pressures is similar . accordingly , these data cannot be used to distinguish between wet loads and dry loads . this may be one reason why those of skill in the art may have believed humidity sensors should not be used to distinguish between wet loads and dry loads as a basis for determining whether hydrogen peroxide should be introduced into a vacuum chamber for sterilization . beginning at approximately t = 0 . 7 minutes , the vacuum pump is deactivated and the vacuum - pump &# 39 ; s valve is sealed to maintain pressure within the chamber until approximately t = 0 . 8 minutes , which allows any residual water to continue vaporizing . then , the modified 100nx ® is vented and ambient air rushes into the vacuum chamber . for the dry load , by approximately t = 1 . 5 minutes , the voltage output from the humidity sensor returns to approximately what it was at t = 0 . however , for the wet load , at approximately t = 1 . 1 minutes , the voltage output from the humidity sensor has reached approximately 3 . 6 volts , which is approximately three times greater than the corresponding values for the wet load and dry load at t = 0 . accordingly , whereas the voltage output from the humidity sensor before pressure in the chamber is lowered cannot be used to distinguish between wet loads and dry loads , there is a distinct difference between the wet and dry loads in the voltage output from the humidity sensor after pressure in the chamber has been lowered and the chamber vented . humidity data , such as the data reflected in fig2 , may thus be used as a basis for determining whether a load is sufficiently dry for hydrogen peroxide sterilization . for example , humidity values on a plot of humidity vs . time corresponding to times subsequent to venting , which may include the maximum humidity value on the plot , may be compared to the baseline value of humidity for a dry load , i . e ., the humidity of an empty chamber or a chamber with a dry load disposed therein that was previously determined when the chamber was at ambient conditions . alternatively , these humidity values may be compared to the minimum value of humidity on the humidity vs . time curve for empty chamber or a chamber with a dry load disposed therein that was previously determined when the pressure in the chamber was lowered to a condition pressure , such as approximately 10 torr . alternatively , these humidity values may be compared to the baseline humidity value at t = 0 and / or the minimum humidity value on the same plot because of the similarity of the humidity plots for wet loads and dry loads before the chamber is vented . whichever type of comparison is performed , a marked difference between the humidity values before and after venting indicates that a load contained residual water . in some exemplary comparisons , a maximum humidity value greater than the baseline humidity value is considered to indicate a wet load whereas a maximum humidity value equal to or less than the baseline humidity value is considered to indicate a dry load . further experiments were performed to correlate relative differences in humidity sensor outputs for maximum humidity values and baseline humidity values with known quantities of residual water within a load . these correlations may then be used to estimate the amount of residual water in other loads in the future . these data are reflected in fig3 . reference numeral 64 corresponds to a dry load . reference numeral 66 corresponds to a load with approximately 1 ml of residual water disposed thereon . reference numeral 68 corresponds to a load with approximately 2 ml of residual water disposed thereon . reference numeral 70 corresponds to a load with approximately 3 ml of residual water disposed thereon . reference numeral 72 corresponds to a load with approximately 4 ml of residual water disposed thereon . reference numeral 74 corresponds to a load with approximately 5 ml of residual water disposed thereon . reference numeral 76 corresponds to a load with approximately 10 ml of residual water disposed thereon . for each set of data , the baseline humidity at t = 0 is similar , i . e ., between approximately 1 . 5 and approximately 1 . 6 volts . the pressure in the chamber starts being lowered at approximately t = 0 . 15 minutes , and a corresponding drop in humidity for each curve is observed . by around approximately t = 0 . 4 minutes , the humidity values for each sample begin overlapping or approximately overlapping . that is , the humidity values for each sample , from the dry sample to the wettest 10 ml sample , are equal or approximately equal . at approximately t = 0 . 7 minutes , the chamber is sealed , at which point the humidity output for each sample is approximately 1 . 1 volts , the minimum humidity value for each curve . an increase in the humidity values is immediately thereafter observed on the 10 ml curve ( reference numeral 76 ). the chamber is vented at approximately t = 0 . 8 minutes . by approximately t = 1 minute , the humidity vs . time curves have each diverged from the others . then , by approximately t = 1 . 1 minutes to approximately t = 1 . 15 each of the humidity vs . time curves corresponding to the wet loads has have reached their maximum humidity values . for the 10 ml curve , reference numeral 76 , the maximum humidity value is approximately 3 . 7 volts . for the 5 ml curve , reference numeral 74 , the maximum humidity value is approximately 3 . 6 volts . for the 4 ml curve , reference numeral 72 , the maximum humidity value is approximately 3 . 4 volts . for the 3 ml curve , reference numeral 70 , the maximum humidity value is approximately 3 . 2 volts . for the 2 ml curve , reference numeral 68 , the maximum humidity value is approximately 2 . 8 volts . for the 1 ml curve , reference numeral 66 , the maximum humidity value is approximately 2 . 2 volts . for the dry curve , reference numeral 64 , the humidity values reach approximately 1 . 4 volts , which is less than the baseline humidity value . these data may be used to determine the amount of moisture introduced into the vacuum chamber in the future . for example , if the maximum humidity value of a load is approximately 3 . 5 volts , it may be determined that the load included approximately 4 ml to 5 ml of residual water . alternatively , the data suggest that if the maximum humidity value is approximately 0 . 5 volts to 0 . 75 volts greater than the baseline humidity value , or approximately 1 . 0 volts to 1 . 25 volts greater than the minimum humidity value , the load may be too wet to sterilize reliably with hydrogen peroxide . accordingly , these data may be used as a basis for determining that hydrogen peroxide should not be introduced into the vacuum chamber until after the load has been dried , either manually or via a load conditioning process . however , if the maximum humidity value of a load is approximately equal to or less than the baseline humidity value of approximately 1 . 5 volts , then the load may be sufficiently dry for sterilization by hydrogen peroxide . accordingly , these data may be used as basis for determining that hydrogen peroxide may be introduced into the vacuum chamber for sterilization . further experiments were performed that confirmed that the above described experiments are repeatable and provide reliable results . in some instances , residual water within a load may be removed from a vacuum chamber by a process called “ load conditioning .” the technology described above may be incorporated into a load conditioning process to help determine whether the load conditioning process is drying a load as intended and , ultimately , whether the load is sufficiently dry for sterilization by hydrogen peroxide . one technique of load conditioning is sometimes referred to as “ vacuum pulsing .” vacuum pulsing typically begins when a vacuum chamber is in a low pressure state and includes some combination of providing energy to a load in the chamber , pressurizing the chamber , and reducing the pressure . building on the techniques set forth above , for example , air may be withdrawn from a vacuum chamber containing a wet load having , e . g ., 5 ml of water therein until the pressure within the chamber reaches a conditioning pressure , p c , of approximately 10 torr . following a dwell time during which the conditioning pressure is maintained , the chamber may be vented . the venting should cause the humidity sensor to output a maximum humidity value of approximately 3 . 6 volts , based on the foregoing description concerning fig2 - 3 . before venting , energy may be provided to the load by way of a plasma or by using heating elements , such as heating elements 26 to further exacerbate vaporization of any residual water . alternatively or additionally , the chamber may be vented to introduce ambient air into the chamber that is warmer than the air presently in the chamber , which may warm the load and residual water thereon . at this point , there should be less than 5 ml of residual water disposed within the load because at least some of the residual water should have been vaporized during the foregoing steps , which is what causes the maximum humidity value to be greater than the baseline humidity value . however , some residual water may remain . again , air may be withdrawn from the chamber , and perhaps energized , before the chamber is vented again . output from the humidity sensor should indicate that some water remained , but that the amount of water that remained is less than the original 5 ml . these steps may be repeated multiple times until the output from the humidity sensor is less than the baseline humidity value . data from a vacuum pulsing process is reflected in fig4 . a plot of data corresponding to humidity vs . time for a wet load containing 5 ml of water that is subject to vacuum pulsing is indicated by reference numeral 82 . a plot of data corresponding to humidity vs . time for a dry load is indicated by reference numeral 80 . the load conditioning process for the wet load begins in a manner similar to the process described in conjunction with fig2 . the first maximum humidity value occurs at approximately time t = 1 . 1 minutes . the first maximum humidity value is approximately equal to 3 . 4 volts , close to the corresponding value of approximately 3 . 6 volts in fig2 . air is then repeatedly withdrawn to a conditioning pressure , p c , which may be approximately equal to 10 torr , and subsequently reintroduced into the chamber by venting the chamber , thereby energizing any water that remains therein . following each venting step , the maximum humidity value is compared to the baseline humidity value to determine if the load was dry . if it is not dry , the vacuum pulsing continues until the maximum humidity value is less than or equal to the baseline value . as shown in fig4 , the sample load having 5 ml of residual water therein was determined to be successfully dried via load conditioning following six venting steps . a low - temperature chemical sterilization system , such as sterilization system 10 , may be designed to perform various routines concerning determining whether any water is in vacuum chamber 12 , whether load conditioning should be performed , and whether hydrogen peroxide should be introduced into the vacuum chamber . an example sterilization process , which includes steps that a sterilization system may perform , such as a routine for determining whether load conditioning should be performed , a load conditioning routine , and a sterilization routine , as well as other steps that a healthcare worker may perform , is set forth in fig5 . this process is set forth only as an example to further illustrate the disclosed subject matter and explain its utility . many of the steps included in this process may be performed alternatively or additionally before or after other steps . the steps set forth in this example may be performed in varying combinations and permutations without departing from the scope of the disclosed subject matter . for example , load conditioning routines may be performed and / or air plasma introduced into the vacuum chamber before any sterilant is introduced into the vacuum chamber . as detailed in fig5 , the example sterilization process begins with health care personnel cleaning non - sterile instruments soiled from prior use using water , washing solution , or a water - soluble instrument lubricant . the instruments are then dried using any or a combination of various techniques known in the art , such as heating the instruments or blowing compressed air into the instruments , particularly lumens of the instrument . the dried instruments may be placed within a sterilization box or rack made from , e . g ., a metal , such as aluminum , or a plastic , such as polycarbonate . the instruments and / or rack are wrapped within a sterilization wrap to form sterilization pack or load 14 . the wrap acts as a barrier to microorganisms , but it permits passage of a sterilant therethrough . once wrapped , the pack is ready to be introduced into the vacuum chamber 12 of sterilization system 10 . a biological indicator may also be disposed within the chamber . the chamber is closed and sealed by closing barrier 16 . at this point , timer 45 is started and control system 38 begins recording humidity data output from humidity sensor 50 at each time increment δt , which may be every approximately 0 . 1 seconds or approximately 1 second . the first humidity data point recorded , which corresponds to time t = 0 and the original pressure in the chamber , which may be equivalent to the ambient pressure , is the baseline humidity value , h b . valve 22 of vacuum pump 18 is opened and vacuum pump 18 is activated . air is withdrawn from chamber 12 by pump 18 until pressure sensor 24 indicates that the pressure in chamber 12 is less than or equal to a predetermined conditioning pressure , p c . p c may be any pressure at which water becomes readily vaporized , for example , approximately 10 torr . once the pressure in chamber 12 reaches p c , pump 18 is deactivated and valve 22 is closed . the pressure in chamber 12 is maintained at p c for a period of time , or dwell time , t d , which may be equal to approximately 0 . 1 seconds , approximately 0 . 5 seconds , approximately 1 second , approximately 5 seconds or approximately 10 seconds . following t d , chamber 12 is vented to atmosphere , perhaps by opening valve 22 without activating pump 18 and / or opening the venting valve . control system 38 and particularly processor 40 check subsequent values of h i to determine whether any such values are greater than the baseline humidity value , h b . in some versions of the process , processor 40 compares only the maximum value of h i , i . e ., h max , to h b . in other versions of the process , processor 40 compares h i and / or h max to the minimum value of h i , i . e ., h min . if no h i is greater than h b , and / or if h max is less than h b , then it may be presumed that load 14 is dry . accordingly , the sterilization cycle of the sterilization process may commence . specifically , valve 22 is opened and pump 18 activated to withdraw more air from chamber 12 until a predetermined sterilization pressure , p s , is achieved in chamber 12 . p s may be approximately 0 . 3 torr , approximately 0 . 5 torr , approximately 1 torr , approximately 2 torr , or approximately 3 torr . once the pressure in chamber 12 is at p s , pump 18 is deactivated and valve 22 closed . an isolation valve between chamber 12 and sensor 50 should also be closed to prevent damaging sensor 50 with hydrogen peroxide . valve 32 is open and hydrogen peroxide from sterilant reservoir 28 is introduced in vapor form , or a liquid form that readily vaporized ( e . g ., droplets ), into chamber 12 . subsequently , chamber 12 is evacuated of hydrogen peroxide and pressurized back to , e . g ., ambient pressure . the chamber is then opened by opening barrier 16 . the instruments , now in a sterile state , may then be removed from within chamber 12 . if , however , an h i corresponding to a time after p c was achieved is greater than h b , a load conditioning cycle may begin . in the process of fig5 , vacuum pulsing is performed by repeating the steps of withdrawing air from the chamber until the pressure has reached p c , maintaining the pressure at p c for t d , venting the chamber , and comparing subsequent h i to h b . as before , if no h i is greater than h b , and / or if h max is less than h b , then it may be presumed that load 14 is dry . if this is not the case , then another round of load conditioning may be performed . load conditioning may be repeated as many times as necessary to dry the load . alternatively , the process may time out and abort if the load is not sufficiently dried within a certain number of conditioning attempts , such as 2 , 5 , 7 , or 10 attempts . it should be understood that any of the examples and / or embodiments described herein may include various other features and / or steps in addition to or in lieu of those described above . the teachings , expressions , embodiments , examples , etc . described herein should not be viewed in isolation relative to each other . various suitable ways in which the teachings herein may be combined should be readily apparent to those of ordinary skill in the art in view of the teachings herein . having shown and described exemplary embodiments of the subject matter contained herein , further adaptations of the methods and systems described herein may be accomplished by appropriate modifications without departing from the scope of the claims . some such modifications should be apparent to those skilled in the art . for instance , the examples , embodiments , geometrics , materials , dimensions , ratios , steps , and the like discussed above are illustrative . accordingly , the claims should not be limited to the specific details of structure and operation set forth in the written description and drawings .
a method of operating a sterilization system having a vacuum chamber for sterilizing instruments , the chamber connected to a reservoir of sterilant by a valve in a closed state , is disclosed . the method comprises placing the instruments in a non - sterile state in a sterilization pack , opening the chamber , placing the pack into the chamber , closing the chamber , withdrawing a first volume of air from the chamber , changing a volume of liquid water into vapor , opening the valve , introducing the sterilant into the chamber , withdrawing the sterilant from the chamber , introducing a second volume of air into the chamber , opening the chamber , removing the pack from the chamber , and removing the instruments in a sterile - state from the pack . the method may also include taking a baseline humidity measurement while the pressure within the chamber is a first pressure , lowering the pressure within the chamber to a conditioning pressure , maintaining the conditioning pressure for a dwell time , increasing the pressure within the chamber , acquiring a second humidity measurement from within the chamber , and comparing the baseline humidity measurement to the second humidity measurement .