CA1329494C - Explosive detection screening system - Google Patents

Abstract

ABSTRACT OF THE DISCLOSURE

An explosive detection screening system used for the detection of explosives and other controlled substances such as drugs or narcotics. The screening system detects the vapor and/or particulate emissions from the aforementioned substances and reports that they are present on an individual or object and the concentration of each substance detected.
The screening system comprises a sampling chamber for the collection of the vapor and/or particulate emissions, a concentration and analyzing means for the purification of the collected vapor and/or particulate emissions and subsequent detailed chemical analysis of said emissions, and a control and data processing system for the control of the overall system.

Description

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1. Pield of the Invention This invention relates to systems for the detection of explosives and other controlled substances such as drugs r narcotics. ~:ore particularly, the present invention relates to an integrated system consisting of a sampling chamber, a detection system, and a data processing system for the detection of the vapor and/or particulate emissions o explosives and controlled substances in a non-invasive ner .

2. Discussion of the Prior Art In recent years there has been a steady increase in the illegal use of explosives 2s well as an increase in the transportation of contraband substances such as drugs or narcutics. It is impossible to detect the existence or prevent all of the cases of bombings and drug smuggling going on; however, it is possible to detect explosives and contraband substances in particular areas where high visibility and/or vulnerability exists such as in airports or airplanes. There are numerous ways in which an individual can place drugs or explosives on an airplane, and even more places an individual can hide the drugs or explosives once on the airplane. The illegal substances can be brought on the alrplane by a knowing or unknowing individual by concealing the substance on his/her person or by placing the substances n baggage to be placed in the cargo section of the aircraft.
The methods for detecting substances such as explosives and drugs or narcotics have been studied for many years, and various techniques have been developed ~hich range ~ ' -2- ~2~

from e~plosives/drug sniffing dogs to highly sophisticated vapor detection devices. Basically, the detection of the aforementioned substances is accomplished in one of two ways;
namely, non-vapor detection and vapor detection. Non-vapor detection methods include x-ray detection, gamma-ray detection, neutron activation detection and nuclear magnetic resonance detection. These methods of detection are more applicable to ~he detection of the various substances when the substances are concealled and are carried or associated with non-living items such as baggage to be carried onto an aircraft in that the detection techniques might pose a threat to living items. Vapor detection methods include electron capture detection, gas chromatography detection, mass spectroscopy detection, plasma chromatography detection, bio-sensor detection and laser photoacoustic detection.
These methods of detection are more applicable to the detection of substances that are concealled and associated with living items such as those that can be carried by individuals including the residuals left on the individual who handled the various substances. All of the above methods are presently utilized, including explosive and drug sniffing dogs.
Today, there are many private and government research studies devoted to the development of systems and methods for the detection of explosives and drugs or narcotics. With the advances in explosives technology, such as the advent of the plastique explosives, which can be disguised as common items, it is becoming increasingly difficult to detect these substances. The problems that must be overcome in the detection of these substances as well as 3 others, include low vapor pressure of the particular vapors escaping from the particular substance, the search time and the throughput of the various systems, the low concentration .

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of the vapor or particulate emissions from the particular subst~nce, isolation of the particular substance with a high degree of reliability, and maintaining the integrity of the systems environment. -There is numerous prior art dealing with the technology of explosive and drug detection devices. The article "Air Flow Studies For Personnel Explosi~e Screening Portals" authored by R. L . Schellenbaum of Scandia National Labs which was published in 1987 as part of the Carnahan Conference on Securities Technology in Atlanta, Georgia (July 15, 1987) discloses a study on various types of integrated systems for the detection of contraband explosives. ~he study outlined a three step process, which includes the collection of vapor, preconcentration,-and detection, for the capture and detection of the vapors eminating from explosive substances. The article discloses various types of collection devices for cGllecting the sample. Various portal configurations and air flow mechanics within each of the portals were studied to see which one provided the best sample. The Atmos-Tech Air Shower Portal, a Modified Atmos-Tech Portal and a Cylindrical Portal were used in the study with various air flow configurations. The study concluded that downward, semi-laminar flow over the body cross-sectional area combined with a vacuum flow collection funnel of approximately twelve inches in diameter placed bëneath the grating in the floor of the portal was the best way to collect the explosives vapor or particulate emissions from an individual passing through the portal.
~ or the detection part of the study, various detection devices were used including the *Phemto-Chem 100 Ion 3 Mobility ~pectrometer in combination with a preconcentrator developed by Ion Track Instruments Inc. The ion mobility spectrometer is a plasma chromatograph which uses an *Trade mark ~ .
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atmospheric ion-molecule reactor that produces charged molecules which can be analyzed by ion mobility. The preconcentrator comprises a motor-driven~ metal screen disc rotated within a cast metal casing. The screen adsorbs the vapor and is then heated for desorption of the vapor. This adsorption-desorption process is the necessary preconcentration step which is used to increase the vapor or particulate concentration in the collected air sample.
The major problem encountered in the use of the portal detection systems in the study was maintaining the integrity of the sample air volume. In maintaining the integrity of the s~mple air volume, it is necessary to prevent the sample air volume to be contaminated with the am~ient environment at the s-ame time trying to maintain a steady flow of traffic through the portal, which is essential to efficient operation of any type of screening system in which heavy traffic is common place. The aforementioned -~
article suggests that the integrity of the sample air volume was not maint,ined in portals without doors. If ambient drafts were present, such as those from air conditioners or just the flow of pedestrian traffic, a reduction of ten percent in detection was encountered. The addition of doors on the portals effected a rise in the detection rate;
however, it produced unacceptable pedestrian traffic problems -which would not meet the requirements for high throughputs required by airports.
In the patent art, there are a group of references which disclose various methods and devices for detecting contraband substances, including both drugs and explosives.
These references are all directed to the detection of ~ -3 contraband substances within a container or luggage, and not those carried on a person. U.S. Patent 4,580,440 and U.S. ;-Patent 4,718,268 both assigned to British Aerospace Public ', ., ' .
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Company Limited disclose a method and apparatus for detecting contraband substances sealed in freight type cargo, sasically~ the method consists of sealing the cargo in a container, agitating the cargo in order to shake off the vapor or particulate matter eminating from the cargo into the surrounding atmosphere, sampling the atmosphere, heating the collected s2mple and analyzing the sample utilizins gas chromatography. U.S. Patent 4,202,200 assigned to Pye Limited discloses an apparatus for detecting explosive substances in closed containers. Basically, objects such as luggase are passed through a controlled axis tunnel wherein the objects are swept by circulating air flows, and then the air sample is collected and analyzed. It is also suggested that if a larger tunnel is constructed, people as well as objects can be passed through it. The aforementioned inventions provide a means and method for detecting contraband substances by using vapor sampling; however, none of the inventions provide or suggest the use of a preconcentrator means for increasing the sensitivity and selectivity of the detection means. Additional patent references which disclose similar type systems are U.S.
Patent 3,998,101 and U.S. Patent 4,111,049.
There are numerous patent references in the testing and monitoring art which disclose a concentration step which includes the filtration or absorption of the molecules of interest over time. After a predetermined period of exposure, the filtering/absorption media is removed and desorbed with heat~ while a new filter/absorption media is placed in the air stream. U.S. Patent 3,768,302 assigned to Barringer Research Limited discloses a system used in the 3 geological testing area and in which the system receives an air stream containing particulates. The sample undergoes a concentration step which includes passing the air sarnple over ; . "ij, . " , ~ r ~ , : . . :, ; , .

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two paths with adsorbing/desorbing steps, and finally analyzed. U.S. Patent 4,056~968 assigned to the same assignee as the above patent also discloSes a Syste~ which is also used in the geological testing area. In this invention, the concentrated molecules could be desorbed from a moving tape as well as from a moving disk. U.S. Patent 4,775,484 discloses a rotating filter media ~hich is used to absorb particulate material during one stage of its rotati~n, and which is purged or cleaned at a separate and second stage of its rotation. U.S. Patent 4,127,395 also discloses a common absorption/desorption circuit uslng a pair of absorbent media, wherein one of the pair is absorbing, while the other is desorhing. U.S. Patent 3,925,022, U.S. Patent 3,997,297 -~ -and U.S. Patent 3,410,663 al~ disclose absorption/desorption -type devices. All of the aforementioned devices disclose systems for the abso-ption and subsequent desorption of particulate or vapor matter; however, none disclose a portal type sampling chiamber.

The present invention is directed to a system for the detection of e~plosives, chemical agents and other controlled substances such as drugs or narcotics by detecting their vapor and/or particulate emissions. The system co~prises a sampling chamber, a vapor or particulate concentrator and analyzer, and a control and data processing system. The system is particularly useful in field environments, such as airports, where it can be used to detect the aforementioned substances on an individual or in 3 the baggage of the individual. The system meets the requirement to detect the aforementioned substances in a non-invasive manner at any required level, and to do it so quickly that the free passage of people and baggage is not unduly interrupted.

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The sampling chamber is a portal with internal 1 dimensions of appro~imately siY. feet in length, seven feet in height and three feet in ~idth. The dimensions of the portal are such as to allow an average sized indiviaual as ~ell as a wheel chair bound individual to easily pass through. The portal is desisned in such a way as to have an internal air flow sweep over an individual walking or passing through the portal at a normal walking pace, and at the same time have the air sample swept from the individual contain a meaningful concentration of vapors or particulate matter to be analyzed. To accomplish this, the sampling chamber or portal is designed with a unique geometry and contains air guides or jets for providing an air flow which effectively isolates the internal air volume from the ambient environment while efficiently sweeping the individual passing through the portal. The air volume or sample inside the portal is collected through a sampling port located within the ceiling section of the portal. The air sample is then transported to the sample collector and preconcentrator (SCAP).
The sampling chamber or portal is capable of collecting and delivering to the SCAP vapor or particulate matter when they are present in as low a concentration as several parts per trillion of ambient air. The SCAP, through a series of steps of decreasing sample volume and increasing sample concentration, delivers a concentrated sample to a fàst response chemical analyzer which may be either a gas chromatograph/electron capture detector or an ion mobility spectrometer or both. The principle of operation of the SCAP
is one of adsorbing the sample onto a selected substrate with subsequent selective thermal desorption. This process 3 is repeated through a series of steps of decreasing sample volume and increasing sample concentration. Upon completion of the preconcentration steps, the purified sample material .

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is analyzed by the aforementioned devices wherein the l analysis consists of identifying the various materials and determining the amount of material present.
The total system and all system processeS are controlled by a control system which comprises a digital computer and associated software. The system is configured and controlled to make all required measurements and prepare the results in a usable and inte11igible format. The control system controls the collection of vapors, the preconcentration and analysis steps, and the data analysis and data formatting. In addition, the computer continuously performs self diagnostics and self calibration procedures on the total system and alerts the user to any potential problems.
~ The system for the detection of e~:plosives and other controlled materials of the present invention provides for the efficient detection of explosives, chemical agents or other controlled materials such as drugs or narcotics by detecting the vapor and/or particulate emissions from these substances. The vapor or particulate emissions can come from substances concealled on the individual, the individuals baggage, or from a residue left on an individual who handled the particular substance. The present invention provides a system with a high degree of sensitivity and selectivity.to a wide range of substances. The high degree of sensitivity and 25 selectivity is accomplished by employing a system which -utilizes the combination of a unique geometry portal with aerodynamics that prevent the cross-contamination of air within the portal with that of the ambient environment and a multi-stage preconcentrator that decreases sample volume 3 while maximizing sample concentration thereby allowing much larger sample volumes to be taken as well as much shorter :~
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sample collection times. The system provides a high 1 reliability rate which is accomplished by utilizing the computer control system for automatic calibration and self diagnostic procedures. In addition, the system provides a high degree of versatility in that by changing the programming of the computer, a wide range of explosives, controlled chemical agents, and drugs and narcotics which have differing physical and chemical properties can be detected. Having the total system under software control provides a more versatile system and one that is easily reconfigurable.
The present invention has a ~lde variety of applications where a high throughput of people is required.
In airports, the detection o~ explosives and controlled substances is of paramount importance due to the rise in terrorist attacks and drug smuggling. The present invention allows for the fast and reliable detection of the aforementioned substances in a non-invasive manner in a variety of field environment such as in airports. The system of the present invention is applicable where the detection of concealled substances is absolutely required.

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For the purpose of illustrating the invention, th~ere is shown the drawings the forms which are presently preferred; however, it should be understood that the invention is not necessarily limited to the precise arrangements and instrumentalities here shown.
Figure 1 is a sectional side view of the sampling 3 chamber of the present invention;

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-lo- ~32~9~ -Fi~ure 2 is a sectional end view of the sampling l chamber of the presen~ invention taken along section lines 2-2' in Figure l;
Figure 3 is a top viet~ of -the sampling chamber of the present invention;
Figure 4 is an end vie~J of the sampling chamber of the present invention;
Figure 5 is a ciasrammatic representation of the flow of air within the sampling chamber of the present invention;
Figure 6 is a diasra~matic sectional view of the internal/external air boundary that eAists at the end of the sampling chamber of the present invention;
Figure 7 is a diagrammatic block diagram of the sample collector and preconcentrator of the present invention~
Figure 8 is a diaqrammatic block diagram of the . .
sample collector and preconcentrator of the present invention with a three filter configuration; ~.
Figure ~ is a plane view of the three filter : :
configuration of the primary preconcentrator of the present invention. -lOB
Figure lOA/is a diagrammatic representation of the multi-port valve used in the present invention;
Figure 1~ is a diagrammatic diagram of the portable 25 sample collector of the present invention; - .
Figure llB is a diagrammatic representation of the luggage sampling means of the present invention;
Figure 12 is a block diagram of the control and data processing system of the present invention; ~;:
3 Figure 13 is a flow chart of the computer program used in the present invention: and Figure 14 is a time chart indicating the various time durations of the processes associated with the screening process.

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' ' The e~plosive detection screening system of the present inve~tion is designed to detect explosives, chemical agentS or other controll~d materials such as drugs or narcotics by detecting their vapor or particulate emissions.
These substances are assumed to be concealled on individuals or in their baggage in airports or in other high vulnerability, high visibility environments. It is necessary to detect these substances in a non-invasive manner at any required level, and to do it so cuickly that the ~ree Dassage of people and baggage is not unduly interrupted. The system is an integrated system comprising a sampling chamber, a vapor and/or particulate concentrator and analyzer and a control data processing system.
The sampling chamber is a portal in which internally generated air flows sweep the vapor znc/or particulate emissions eminatins from an individual or object passing through the chamber to a collection area. The sampling chamber is designed in such a way as to capture a high enough concentration of emissions so as to be able to detect the presence of the aforementioned substances with a high degree of reliability and dependability. The internal volume of air is recirculated with a small amount being removed at the sampling time. At the sampling time, an external air pump or fan draws a sample of the collected air volume into a sample collector and preconcentrator (SCAP).
The sampling chamber is capable of collecting and delivering to the SCAP, vapors when they are in as low a concentration as several parts per trillion of ambient air. `
3 The SCAP, through a series of steps of decreasing sample `
volume and increasing sample concentration, delivers a concentrated sample to a fast response chemical analyzer : .. ; . ~ .: ,, . ~ .. .. . . . .

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which may be either a gas chromatograph/electron capture l detector ox an ion mobility spectrometer or both. Using this multi-stage concentratiOn process of adsorption and desorption, much larger sample volumes can be processed with high degrees of sensitivity and selectivity. The data collected is then assimilated and analyze~ by a digital computer which is part of the control s~stem which operates and controls the total system.
The control system is a control and data processing ~-system of which the primary requirement is to reDort the presence of, and if required, the level of a speci'ied substance. The system must be capable of distinsuishing between background levels of a substance and alarm levels.
The system also controls the operation of the entire system by automatic control metho*s which is run by a microprocessor or digital computer. The control system is easily reprogrammed to detect various substances because of modularized programming techniques.

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The sampling chamber for people is a portal that is designed in such a way that as a person walks throush this chamber, at a normal walking pace, an internal air flow carries a sample of vapors and/or particulate matter from them to a sampling port where it will be collected for analysis. There are three major design requirements that the -chamber was designed to meet. First, the sampling chamber must gather a meaningful sample of the environment surrounding a person or object passing through the chamber.
3 In considering a solution to the problem posed by the first design requirement, it is necessary to consider that the sampling chamber must be large enough 'or an average size ~ .' -13- 1329~

individual to comfortably pass through the chamber;
l therefore, there is a considerable volume of air located within the chamber resulting in possibly only several parts vapor or particulate emission per trillion parts of air or possibly even less. The solution to this problem of dilution is to design the chamber long enough so the individual or object passing through the chamber remains in the chamber for a duration of time so as a meaningful sample of the environment can be gathered. Second, for the purposes o' sensitivity, selectivity and preventing cross-contamination of the sample to be analyzed, the sample to be collected must be isolated as much as possible from the ambient enviro~ent.
In considering a solution to the problem posed by the second design requirement, it is necessary to once again consider the problem of dilution caused by having a larger chamber.
Since there already exists a dilution problem, the chamber must be designed with a unique geometry and in'ernal aerodynamics so as to prevent further dilution and contamination by the mixing of internal air with the ambient air to the greatest extent possible. The third design requirement is that the sample must be gathered in as complete form as possible in as short as time as possible.
In considering a solution to the problem posed by the third design requirement, it is necessary to consider the problems and solutions considered above and find a balance between them. The time an individual or object spends in passing through the chamber must be long enough so as to gather a meaningful sample, but not long enough to cause unduly long - pedestrian traffic delays. Secondly, since there is a dilution problem, the chamber was designed in a unique way 3 so as to prevent cross-contamination with the ambient environment, and this unique design must not prevent the -': ' .

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normal flow of traffic; ther~fore, the aerodYnamics discussed l in the solution to the second problem must be such that the meaningful sample is gathered quickly.
Referring to ~igures 1 an~ 2, there is shown a s~ctional side view and end view or the sampling chamber 100 or portal. The sampling chamber 100 has a rectangular geometry having internal dimensions of app_oximately six feet in lensth, seven ~eet in height, and three feet in ~idth.
These dimensions allow an average size individual, walking at an normal walking pace to remain in the chamber 100 for approximately two to three seconds which is enough .ime to gather the aforementioned meaningful s~r.ple. The rectangular chamber 100 has two ~7alls 102a and 102b, 7hich run the le~gth of the chamber 100, a floor ~04, a convergent or conically shaped ceiling 106 the importance of which will be discussed 15 subsequently and a roof 107. In order to maintain the ;
uninhibited flow of pedestrian trafric through the chamber 100, no doors and only two walls, 102a znd 102b, were used.
Hand rails 108a and 108b attached to walls 102a and 102b respectively are provided to aid individuals in passing through the chamber 100 quickly and safely. The floor 104 of the chamber 100 is not a necessary component, and in other con~igurations it is not utilized. The chamber lO0 can be constructed utilizing a variety of materials including aluminum and plas ics; however, clear materials such as *plexiglass or ~iberglass is pre~erred 80 individuals passing through the chamber 100 can be observed. In addition, a video camera 109 may be utilized to capture an image of the individual passing through the chamber 100 which will be electronically stored along with the collected data.
3 The sampling chamber 100 operates on an air recirculat~ng principle and the only air removed from the internal recirculating volume is a comparatively small amount . , :
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leaving by sampling port 118a. The internal air volume is 1 circulated through internal air flow guides or jets and is collected by collection duct 110 which is a 16" x 20" x 6"
rectangular duct connected to the center Oc the conical ceiling 106 and which empties into the space created between the ceiling 106 and the roof 107. ~his results in a large volume of controlled recirculating air flow cap2ble of delivering a vapor and/or particulate sample from anywhere in the chamber 100 to the sampling port 118a in approY.imately one second.
The conical ceiling 106 aids in the collection of the sample volume by creating an inverted funnel for the air sample flow which serves to concentrate a larger volume of air across a smaller cross section for sampling purposes. A
dynamic low pressure zone is created in the region of the collection duct 110 when the air is drawn through the collection duct 110 into the ceiling plenum by four eAhaust fans two of which are sho~n in Figure 2 as 114, and 114a. In each corner of the chamber 100, there are six inch diameter end columns 112a-d. Each of the four end columns 112a-d are mounted vertically in the chamber 100 and run from the floor 104 to the ceiling 106. Each column 112a-d has six slots of one foot in length and a half inch in width 113a-d as shown in Figure 3, which is a top view of the chamber 100, with inch and a half internal guide vanes (not shown) for directing the air flow at a forty-five degree angle towards the center of the chamber 100 as shown by arrows 115a-d in Figure 3. The air flow through the columns 112a-d is provided by four independent fans, two of which are shown in Figure 2 as fans 114 and 114a. The four fans are mounted in 3 the chamber 100 above the conical ceiling 106 and below the outer roof 107. Each fan is connected to one of the end columns 112a-d and provide 1000 CFM of air to each column - -16- ~ 32~

112a-d resulting in an air velocity of 17m/sec, in the 1 directions indicated by arro~s llSa-d, from the guide vanes of the columns 112a-d as shown in Figure 3. The suction side of the fans are open to a com~on plenum located in the same space that the fans occupy. In addition to these inwardly directed vertical air jets 113a-d there are two upwardly directed air guides 117a and 117h or jets located in side air flow pipes 116a and 116b which are mounted along the floor 104 and against walls 102a and 102b. The side flow pipes 116a and 116b are connected to end columns 112a-d and receive air rrom them; In each side flow pipe 116a and 116b there are twelve inch by half inch air slots 117a and 117b located in the center of each pipe and directed towards the center of the chamber at a forty-five degree angle as shown in Figure 4. The air velocity of the air leaving side flow pipes 116a and 116b is lSm/sec in the direction indicated by arrows ll9a and ll9b. The combined effect of the air flow created by the end columns 112a-d and the side flow pipes 116a and 116b is a dynamic high pressure region created in the center region of chamber 100. ~he recirculating fans which draw air through collection duct 110 create a dynamic low pressure zone within chamber 100, which creates a net air flow up towards the collection duct 110. This air flow is the flow that sweeps individuals or objects passing through the chamber. The effect of the high pressure region and the low pressure region created by the exhausting air sample through conical ceiling 106 and into the collection duct 110 i.s a balance of atmospheric conditions which results in very little external air entering or leaving the chamber 100. Basically, the high pressure region inhibits air from entering the chamber 100.
3 The majority of the moving air mass goes through the collection duct 110 and to the common plenum where it will ~ ' . --17- ~ 3~
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once again be used by the fGur fans to recirculate the l internal volume of the chamber lO0. ~ portion of the recirculated air is collected through a sampling port 118a, which is the open end of a stainless steel pipe 118 which is used to transport a selected sa~,ple from the cha~er lO0 to the second stage of operation; namely, the preconcentration stage which shall be discussed subsecuently.
The four end columns 112a-d and the two side air flow pipes 116a and 116 represent one embodiment for delivering the air supplied by the four independent fans as separate and directional air jet streams. The fans can be connected to various types of air ducts or plenums with guide vanes or nozzles to form the e~iting air into jet streams.
In addition, partioned hollow walls also with guide vanes or nozzles can be used as an alternate approach for forming the air from the fans into separate and directional air jet streams. The manner in which the air flow is supplied to the guide means and the manner in which the jet streams are formed is not critical; however, the specific directions of the jets streams are. It is important that the proper angle and orientation of the jet streams be maintained so as to provide a net fiow of air capable of sweeping an individual or object passing through said sampling chamber means lO0 while maintaining the integrity of the volume of air within the sampling chamber means 100.
~ Referring now to Figure 5, the volume of air 120 enclosed by the dashed lines indicates the total volume of air moving towards the collection duct 110 and sampling port 118a shown in Figure 2. The upward flow of air starts at approximately one foot in from the perimeter of the chamber 3 floor 104. Ihis figure indicates the net upward flow of air, and does not intend to exclude other air currents present in the chamber, because other currents are present; however, ' , ' ,., ' ' ' ~. ~ ' ,'~ --- ~32~9~
their direction is not upward. As can be seen in Figure 5, the effect of the generated internal air flows and the shape of the ceiling 106 shown in Pigure 2 tends to focus or concentrate the large volume of air flo~7ing up~7ards to a smaller, but more concentrated volume of air. Arrows 122a-c, 124a-c and 126a-c indicate the velocities of the air mass at different stages in the flo~7. In the lo~7er to middle regions, the air flo~7 is 2-3 m/sec, and as the air mass approaches the low pressure region, the velocity increases to 4-5 m/sec.
Turning to Figure 6, a diagrammatic side view of the chamber 100 is shown. The region indicated by the dotted lines 128 and 130 indicate the region in which cross-contamination of the internal air volume with the ambient environment occurs. As indicated by arro~s 132a-c, air from the surrounding environment enters the chamber 100 at approximately 0.5 m/sec. The air from the outside environment is drawn in by the aerodynamics created by the internal air flow. This air flow into the chamber 100 results in one half of the internal air to be exchanged with the outside air in approximately 30 seconds. Since the collection time take approximately one second, the cross-contamination is minimal. The only way to maintain absolute integrity of the internal air volume is to provide rotating -doors with a seal, and this however, would result in uAdesirable time delays.

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The sample collector and preconcentrator (SCAP) is 3 used as part of the overall system to enchance overall system sensitivity and selectivity. In general terms, the SCAP must simply discard, in a multi-step process, non-required .

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molecules of air while not losing the targeted molecules of interes~. In the sample collection and preconcentration step, the targeted materials are adsorbed onto a selected substrate, and then selectively desorbed. This process is repeated through a series of steps which decrease sample volume and increase sample concentration.
As illustrated in Figure 7, the SCAP 200 is supplied with sample air by pipe 118 which e~tends to the sampling chamber 100. During sampling periods 2 high suction fan 202 draws the sample volume through the sampling port 118a. The fan 202 is connected to pipe 118 on the suction side with the discharge side connected to a vent or exhaust system to the ambient environment.
The first stage of the concentration process involves the primary preconcentrator 201 which consists essentially of a rotating filtering means 204. The air sample drawn from the sampling chamber 100 is drawn through filtering means 204. The filtering means 204 consists of two interconnected filtering elements 206 and 208. The filtering elements 206 and 208 are wire screens which hold an adsorbing material. Each filtering element 206 and 208 may be rotated through either of two positions. Position 1 is in line with pipe 118 and position 2 is in line with a secondary preconcentrator 203. The positions of the filtering elements 206 and 208 are changed by a control system which in this embodiment is a hydraulic actuation system 210 which is connected to filtering means 204 by shaft 212 which lifts movable platform 211 to move each of the filter elements into a sealed connection at position 1 and at position 2. A
preconcentrator control unit 214 is also connected to 3 filtering means 204 by shaft 216. The hydraulic actuation system 210 is comprised of a hydraulic control unit 210a and a hydraulic pump 210b and is operable to lower and raise holding elements 205 and 207, into the unlocked and ~ :

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locked positions respectively. When it is time to rotate the 1 filters 206 and 208 hydraulic actuation system 210 lowers holding elements 207 and 205 .hich engage filter ele~ents 206 and 208 respectively. Upon engaaement o. the filter elements 206 and 208 preconcentrator control u~it 214, whlch is a computer controlled stepp~r motor is operable to rotate filtering elements 206 and 208 between positior.s 1 and 2 via shaft 216. The control of the hydraulic actuation system 210 and the preconcentrator control unit 214 is acco~plished via the control system ~hich will be fully e~:plained in subsequent paragraphs.
In a second embodiment the filtering means 204 consists of three interconnected fil ering elements 206, 208 ~ -and 209 as shown in Figure 8; Filter element 209 like filter elements 206 and 208 is a wire screen which holds the 15 adsorbing material. Each filtering element 206, 208 ar.d 209 -may be rotated through either of three positions. Position 1 is in line with pipe 118, position 2 is in line with a secondary preconcentrator 203 and position 3 is exactly in between position 1 and position 2. Figure 9 shows a plane view of the three filter elements 206, 208, and 209 spaced 120 degrees apart on movable platform 211. The positions of the filtering elements 206 208 and 209 are changed by a control system which in this embodiment is a hydraulic ~-actuation system 210 which is connected to filtering means 204 by shaft 212 which lifts movable platform 211 to move each of the filter elements into a sealed connection at position 1, into a sealed connection at position 2 and at position 3. The hydraulic actuation system 210 is comprised of a hydraulic control unit 210a and a hydraulic pump 210b -3 and is operable t:o lower and raise holding elements 205, 207 and 215 into the unlocked and locked positions respectively.
When it is time to rotate the filters 206, 208 and 209, hydraulic actuation system 210 lowers holding elements 207, 205 and 215 which engage filter elements 206, 208 and 209, ~ .
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respectively. Upon engagement of the filter elements 206, l 208 and 209, preconcentration control unit 214, which is a computer controlled stepper motor, is operablé to rotate filtering elements 206, 208 and 209 between positions 1, 2 and 3 via shaft 216.
Xeferring now to Figure 7, the two filter process is described. During a sampling period which is controlled by the control system, fan 202 draws the sample îrom the chamber lO0 and through filter element 206 which is position ~ -1. Filter element 206 collects the vapor and/or pa-ticulate matter contained in the air sample on an aasor_tion substrate. The filter element 206 comprises an adsorber that is selected to have enhanced adsorption for the target materials and lessor adsorption for any contaminants. When the air sample passes through the filter element 206 containing the adsorber, the adsorber pre erentially selects a sample of the target materials, and other contaminants are passed on to be vented or exhausted by fan 202. Upon completion of the sampling period, and adsorption of the target materials onto filter element 206, filter element 206 is switched to position 2 by the preconcentrator control unit 214 and raised into a locked position by the hydraulic actuation system 210 so the desorption of the target materials can occur.
In the desorption process, a stream of pure gas is -~
passed over the adsorber containing the target materials and any remaining contaminants. The pure gas, which is usually -an inert gas, is supplied from a gas supply 218 and transported to position 2 of filter means 204 by gas line 220. This pure gas flow is much smaller then the volume of 3 air used in the sampling chamber 100. The temperature of the ads~rber is raised in a controlled fashion by the control system, illustrated in Figure 12. The temperature of the ~ -' ~

~L32~
filter being desorbed is raised by either a heat e~:changer 1 213 or by the temperature of the pure gas from source 218.
If the temperature of the filter being àesorbed is raised utilizing the pure gas, then the gas flow is diverted to a heating element (not shown) where it is raised to the proper temperature. When the desorption temperature for the target material is reached, the temperature is held constant and the pure gas flow is quickly switched to the desorption stage in the concentration process. The heated gas then absorbs the target materials and carries them on to the next stage. The gas flow containing the target materials is routed to the secondary preconcentrator 203 or interface unit via gas line 222. As the desorption process is rapid, only a small volume of gas is transferred which Eesults in the next stage receiving the target materials in a concentrated form.
The primary concentration of the target materials is a continuous two step process because of the two filter elements 206 and 208 both contain adsorbing subs'rates. When filter element 206 is adsorbing the target materials, filter element 208 is in the desorption process. Upon completion of the desorption of the target materials from element 208, the adsorbing material of element 208 is purified from materials and contaminants and thus ready to be used as the adsorber in position 1. While a pair of rotating filter elements is illustrated in Figure 7, it would also be possible to use single use strip media which traverses from the absorbing station to the desorbing station, or to hold the position of the filters fixed and alternate the sample and purge air streams to absorb and desorb the target materials.
Referring to Figure 8, the three filter process is 3 now described. In a second embodiment for the primary preconcentrator 201, a third filter element 209 is added, thus making the primary concentration of the target materials ' ,' , -23~ 132~

a continuous three step process, because the three filter l elements 206, 208 and 209 all contain adsorbing substrates.
When fiLter element 206 is adsorbing the target m~terials, filter element 208 is in the desorption process, and filter element 209 is be added to provide for a thermal cleansing of any vapors or particulates which may remain after the desorption process. l~hen a particular filter element is in position 3, the pure gas supplied from gas supply means 218 is routed to position 3 of filter means 204 by gas line 220.
The gas flow further sweeps the particular filter element in an attempt to further purify the adsorbing materi~l from contaminants. The exiting gas with contaminants is exhausted -~
to the ambient environment. A valve 217 is located in line with gas line 220 and is operable to switch the gas flow from position 2 to position 3 and vise versa.
The treatment of particulates and gaseous materials is slightly different at the first step of the concentration -~
process. The particulates may be small particles or droplets ~ -of the tarqet material itself or small particulates or droplets attached to dust particles or other vapor droplets.
For particulates, the first stage is a filter or screen having selective adsorption characteristics in the path of the sample air flow from the sampling chamber 100. The particulates are physically trapped or adsorbed on this filter, and then the filter, or a portion of it, it physically transferred to a heated chamber and rapidly heated to a temperature that is sufficient to vaporize without -decomposing the target particulates. A small quantity of heated pure carrier gas is admitted to the chamber to carry the now vaporized material to the next stage of the process.
3 As stated previously, the heated gas can be used for supplying the heat for vaporization.

, -24- ~2~4 It is usually the-case that the filter used in the 1 sampling air flow for particulate materials is also the absorber for gaseous materials and therefore, as is show~ in Figure 7 a single primary preconcentrator 207 can be used to capture both particulate materials and gaseous materials. It lS necessary to sample target materials as pariiculates because certain target materials may have too low a vapor pressure at room temperature to be sampled as gas or vapor.
In addition, it is possible that the target material itself has a tendency to be present in the sample volume as an adsorbate on particulate material independent of vapor pressure considerations.
In the subsequent stages of concentration the selectable adsorbers are fixed and confined to metallic tubes. The sample and purge carrier gas flows are manipulated by switching valves which are under computer control. Referring once again to Figure 7, the primary preconcentrator 201 is connected to the interface 203 by gas flow line 222. The interface 203, contains a secondary preconcentrator 224 and a multiport valve system 226. The purpose of the multi-port valve system 226 is for switching between the gas supply line 230 which is supplied by gas supply 228, the preconcentrator 224 adsorption tubes, the gas flow line 222 from the primary preconcentrator 201 and the gas flow line 232 to the chemical analyzers 234 and 236.
Basically, the multi-port valve system 226 is a switching network. The secondary preconcentrator 224 is a series of adsorption tubes. The multi-port valve system 226 is driven by an interface control unit 238 which is simply a stepper motor to rotate the valves in the multiport valve system 226 3 when commanded to do so by the computer. The interface 203 represents a generic block of secondary preconcentrators, and -25- 132~

thus one can cascade a series of multiport valve systems and i adsorption tubes in an attempt to further purify the sample to be analyzed.
The adsorber tubes are very rapidly heated to and held at the selected predetermined temperature by heating the surroun~ing metallic tube. This is usually done by passing a controlled electrical current through the tube and using the tube itself as the heating element. In the case of 12rser adsorbent containing tubes, for the heating times of tens, to a very few hundreds of milliseconds, this current may be several hundred amperes. The temperature maybe measured by brazing a tiny, very low mass thermocouple or thermister to the tube. The thermocouple must be small enough so as ~ot to affect the tube in any manner and it must be capable of - -responding rapidly. The thermocouple feeds the measured temperature to the computer of the control system wherein the computer controls the amount of current flowing through the tubes. Basically, the computer forms the digital closure of -an analog control loop. The computer is used to monitor and control the temperature because the proper thermal program for the desired target materials or material is critical.
The size of the tubes is decreased in steps to reflect the decrease in volume of gas containing the samples and may eventually reach the internal size of a capillary gas chromatograph column~
, The multiport valve system 226 is a switching network with multiple ports as the name suggests. In one embodiment of the present invention, the multiport valve system 226 is a 6-port valve. Figures lOA and 10~ represent the two positions that the 6-port valve 226 can occupy. The 3 interface control unit 238, is a stepper motor, and is -operable to switch the 6-port valve 226 between the two positions. In either position, only pairs of ports are ,.

': :.
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26 ~32~
.

:. , connected. In position l, illustrated in Figure lOB, ports 1 1 and 2, 3 and 4, and 5 and 6 are connected, and in position 2, ilLustrated in Figure lOA, ports 2 and 3, 4 and 5, and 6 and 1 are connected. Position 2 places the adsorb-desorb tube 248 in the load position. The gas flow line 222 shown in ~igure 7 carries the gas containing ~he target material and some contaminants into port 1 indicated at 242 in Figure lOA
of valve 226 wherein the gas automatically flows through an internal passageway 244 to port 6, indicated at 2~6 in Figure lOA. Connected between port 6 and port 3 is an external adsorption/desorption tube 248 in which the gas containing the target material and some minor contaminants pass through.
The adsorbing material inside the tube 248 is specifically targeted for the target material; therefore, the carrier gas and the contaminants flow through the tube 248 to port 3, indicated at 250 while the target material is adscrbed within the tube. The carrier gas and contaminants flow from port 3 indicated at 250 in Fisure lOA to port 2 indicated at 252 in Figure lOA through internal passageway 254, and is vented to the external atmosphere through exhaust line 256. Pure carrier gas supplied from gas supply 228 shown in Figure 7 is fed into port 4 indicated at 258 via line 230. The pure carrier gas automatically flows from port 4 indicated at 258 to port 5 indicated at 260 via internal passageway 262~ The carrier gas then flows from port 5, indicated at 260 to eIther of the chemical analyzers 234 or 236 via line 264.
The analyzers 234, 236 require a continuous gas flow to remain operational. The use of multiport valve systems allows pure carrier to be fed gas continuously to the analyzers 234, 236, even when the adsorb/desorb tube 248 is 3 in the adsorb cycle.
At the end of the adsorption cycle, the computer of the control system then automatically switches the 6-port ~ . . . .. . . .

`` 132~91~
:` -27-valve 226 into position 1 which is the desorb mode as shown in ~igure lOs. Port 1, indicated at 242 in Figure lOB still receives gas from the primary concentrator 201 via line 230;
however, the gas flows from port 1, indicated at 242 to port 2, indicated at 252 via internal passageway 268 and is vented to the atmosphere via exhaust line 256. Port 4, indicated at 258 is injected with pure carrier gas from supply 228 via line 230 which flo~7s to port 3, indicated at 250 via internal passageway 270. As stated before, port 3, indicated at 250 and port 6, indicated at 246 are connected via an e~ternal adsorption/desorption tube 248; however, in this position, the carrier gas is flowing through the tube 248 in the opposite direction. Therefore, when the tube 248 is heated to desorption temperature, the gas will sweep the desorbed target material and czrry it to port 6, indicated at 246 free of atmospheric contaminants. From pGrt 6, indicated at 246, the target material flows to port 5, indicated at 260, via internal passageway 272 and to the chemical analyzers 234 and 236 via line 264.
The external adsorption/desorption tube 248 is electrically insulated from the valve body and contains a selected quantity of the adsorbing material which has the .
best characteristics for adsorbing the target material. High current connections are made to the ends of this tube 248 and are shown in Figures lOA and lOB as electric lines 280 a~d 282. Lines 280 and 282 are connected on the other end to ~ ~ .
a controlled current source 281. A thermocouple 283 is shown attached to tube 248 in Figures lOA and lOB. This thermocouple 283 as stated previously, is used to raise the temperature of the tube 248 so as to achieve the proper .
3 temperatures for desorption. The gas sample which contains the target material, contaminants and excess gas, passes through the tube 248 and because it is cold, and the adsorber .
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-28- 132~

material has been selected to be a strong adsorber for the 1 target- material, most of the sample will be adsorbed at the end of the tube 248 near port 6. The contaminants are less strongly adsorbed and thus any adsorption of them will be throughout the length of the tube 248. Also, because the contaminants are not strongly adsorbed a larger portion of them will pass through the tube to the exhaust vent 256 and be discarded.
A desirable property of thermal deso-ption of gases or vapors on solid or liquid substrates is that the process can be highly thermally sensitive and thermally dependent~ At a specified temperature the amcunt of any material desorbed is related to its physical and chemical propexties and the physical and chemical properties of the adsorbing material. It is possible to choose adsorbing materials such that the contaminating materials are desorbed at a workable lower temperature than the target materials.
Careful thermal programming allows one to use these properties. An example is to heat the desorber tube 248 in a controlled fashion with the valve 226 in position 2. The contaminants such as water vapor etc. are not strongly adsorbed and â low temperature will cause â major portion of them to leave the adsorber and pass out of the system through the vent. At the same time, the target materials will not be desorbed and will remain at the end of the adsorber tube 248 adjacent port 6. If the position of the rotor in the 6-por).-valve is now changed to the 1 position, two important changes are made. The adsorber tube is now connected to the next -stage in the sequence and the pure carrier gas flows through the adsorber tube in the opposite direction to the previous -3 gas flow direction. A rapid controlled increase in temperature will now cause the sample to be desorbed in a short period of time. This results in a sample which has been purified by the previously described adsorption and :' .
: .~ ' ., ~ ` . .".. :.

2 ~

.. ..
desorption process passing to the ne~t stage in the process, 1 contained in the minimum of pure carrier gas. Thus the sample has been twice purified of contaminant5 and concentrated in a much reduced volume o pure inert carrier gas.
The next step in the purification and concentration process may be another 6-port valve with a smaller diameter desorption tube. The final desorption tube should match in diameter the size of the column in one of the analyzers, such as analyzers 234, which is a gas chromatograph. If this is done, it results in ideal sample injection into the gas chromatograph. In fact, it is possible by careful design and construction to have the desorber tube the same internal diameter as a capillary gas chromatograph column. It is possible to use the tube connecting two 6-port valves as a desorber tube for purification and concentration purposes.
It may be packed with adsorber and fitted with heating and temperature measuring equipment such as electrical ;
connections and thermocouples.
The adsorbent material used in the various staqes of concentration of the target materials may be selected from a group of materials commonly used for vapor sampling including *Texax and *Carbotrap. There are other adsorbing materials that can be used with the present invention depending on the particular materials that are to be detected 25- and isolated.
The SCAP also 200 contains an attachment for a portable sampling device 2g2 which is shown in Figure llA.
The connection is a pipe 223 which is connected to pipe 118 shown in Figure 7 or 8 through valve 221. The pipe 118 3 may be stainless steel, aluminum or even ABS plastic.
Basically, the portable sampling device is a hand held wand which when valve 299 closes off the chamber 100 and valve 221 is opened end of pipe 118 and fan -*Trade mark ... ~
-3.

- _30_ ~32~

202 draws an air sample, the wand 2g2 is capable of drawing 1 vapor and/or particulate emissions from a specific area on an individual or object. The wand 292 is used to sample an individual intensively when the results from the pass through the chamber 100 are inconclusive.
A second use for the hand held wand 292 ~ould be to dra~ vapor and/or particulate emissions from baggage that is going to be stored in the cargo hold of the airplane. The system including the hand held wand 292 has proven very effective as a means of detecting explosive vapors in packages and baggage. In tests ~Iherein the hand held wand 292 has been held against cardboard box pac~ages znd various types of luggage, positive indentifications of low levels of explosive vapors, equivalent to approximately a third of a stick of dynamite, are made. In addition, the hand held wand 292 can be attached to a sampling box 294 as shown in Figure llB that is placed over luggage to enhance the efficiency of detection and provides a means to automate baggage screening by including a conveyor belt 298. The wand 292 is attached to sampling box 294 through connection means 296.

The analysis of the purified target material consists of identifying the materials and of determining the amounts present. Because the original concentrations were so low with respect to many other common ambient materials it is possible for there to be, even under the best of purification -and concentration systems, some remaining impurities of materials with similar characteristics to the target 3 materials. Thus the analysis system must be capable of separating the target material response from the response due to interfering materials.

-31- 1 3 2 9 ~r 9 4 Two forms of analysis systems are used either 1 separately or in combination, These systems are an ion mobility spectrometer (IMS) ~36 based analysis system and a gas chromatograph (GC) 234 based sysiem. The final detector for the GC 234 is usually a electron capture detector (ECD) but the IMS 236 can also be used as the detector if desired. Depending on the the application, a photo ioniæation detector or a nitrogen-phosphorus detector or some other detector may be also used following this. The GC 234 may be of the "packed column" type or the capillary column type. Both analyzers 234 and 236 can be used separately or in a combined fashion. Valve 235 is used to direct the collected and purified sample to either or both of the analyzers. -Whatever analysis system is used the analysis must -be completed in a time that is short enough that the free flow of people, luggage and baggage is not unduly inhibited.
This also implies that the time for the concentration and purification process is short as well.
If all the valves in the system are motor driven or solenoid driven valves, the flow directions timings and magnitude may be controlled and varied. The time and temperature parameters are controlled and variable. Thus the ~;
physical characteristics of the complete system may be adjusted to detect a wide range of target materials and the sensitivities may be adjusted to accommodate a wide range of threats as perceived by the authorities using the system.
All the process involved in the collection and concentration as well as the final analysis of the collected material is controlled by the computer of the control and -3 data processing system and will by fully explained in the following section.

-32- 1~2~9~
i The primary requirement for the control and data procesSing system of the screening sys-tem is that it reports the presence of, and if required, the level of specified substances. This means that the equipment must be configured and controlled to make the required measurement and it also means that the result must be presented to the user in a usable form. The subject or target materials may be present in varying amounts in the environment of the system and therefore, the system must be capable of distinguishing between this background level and an alarm level. It may also be a requirement to report on this backsround level.
A secondary requirement for the control and data processing system of the integrated system is self diagnostics, as there may be considerable time between alarms, the control and data processing system must be capable of performing confidence checks that are satisfactory to the operator on demand. There must also be routine self checks and calibration procedures performed on the total system by the control and data processing system.
Basically, this ensures that the test results, wAether positive or negative, must be believable.
A third requirement for the control and data processing system is ease of reconfiguration and versatility.
Th`e range of target materials may be changed from time to time, and the system must be capable of varying its internal operation parameters under program control to detect these materials. ~t is desirable that the rigor of the measurement in terms of time constraints and number and types -3 of substances detected be alterable in an expeditious fashion at any time. The user's requirements in terms of level of ~ 3 2 ~

threat and types of materials may quickly change and the 1 equipment must respond to these changing needs.
The final requirement for the control and data processing system is that the parameters and operations of the sampling chamber and the SCAP must be m,onitored and controlled. This means that all internal timings, temperatures and mechanical components must be controllable by the control and data processing system.
Tne primary method of achieving these requirements -is to put the total system under the control of a stored program digital computer. This computer through a series of modularized software routines performs the data analysis and presents the results in the required form to the ùser. The computer ~hrough another series of modularized software routines continuously performs self diagnostics and self calibration procedures on the total system, and alerts the user to any potential problems. The computer through still another set of modularized software routines controls all the processes of the total system and shall be more fully explained in subsequent paragraphs.
One primary benefit of this system of control is reliability. By themselves the components are rugged and reliable and not prone to failure. However, any system made up of many items is subject to drifts due to ambient changes and-time. By having all components under program control and by arranging for a known input to the system such as a controlled injection of target material or target simulant, there can be a calibration and self-diagnostic program. The function of this program is to calibrate the entire system and determine and store the required time, temperature etc.
3 parameters. If these parameters are not within specified limits for any reason, the program can alert the user.
Guided by a service program the user response can range from ' ', .

- - - .

-34~

immediate shutdown to scheduling service at a later date, to simpl~ noting the circumstanceS By use of a modem this information can be easily transmitted to any~here in the world. The other aspect of reliability in a system of this type is that the user must kno~t that the system is reliable.
Hopefully there will be very long periods of time bet~!een actual alarm events. However, if there is a calibraiion and self diagnostic program and associated hardware for realistic sample injection, the user can generate, at anytime, an actual/simulated alarm event as a confidence check -The second primary benefit of this system of control is versatility. It is advantageous for the system to have the capability of detecting a ~ide range of e~plosives, a range of controlled che~lical agents, drugs, and narcotics etc. All these materials have differing physical ~nd chemical properties. These properties give rise to a set of internal parameters for optimum detec,ion. However ,hese parameters will be less than optimum for some other materials. ~ut, if these parameters are all controllable and easily changed such as by simply reading in or activating a different program in the computer memory, then the user can effectively change the system to meet what is considered to be the threat at that time without making any hardware changes.
Referring now to Figure 12, there is shown a block diagram representation of the control and data processing system 300 and its associated peripheral elements. The digital computer 302 or processor is an AT type personal computer running at lOMHz and has a standard video display ~-terminal 304. The computer 302 is responsible for process -3 control, data acquisition, data analysis and display of results. In addition, as mentioned previously, the computer 302 also contains software routines for self diagnostics and ~.

-35- 1~2~

self calibration procedures. The computer 302 receives power from the power distribution unit 306 as does the sampling chamber 100, the hydraulic pump 210b which supplies hydraulic pressure for the hydraulic control unit 210a, and the process control unit 308. The process and control unit 308 under the control of the computer 302 interfaces and provides the necesSary signals to run the hydraulic control unit 210a, the preconcentrator control unit 214 and the interface control unit 238.
The process and control unit 308 is a standard interface unit between computer 302 and the various actuato~s. The hydraulic control unit 210a controls a hydraulic piston which travels up and do~n to unlock and lock the filter elements 206 and 208 of the primary preconcentrator 201, as sho~n in Figure 7, so they can be rotated from position 1 to position 2 as described in the previous section. Under software control, the process control unit 308 outputs com~ands to a two-way solenoid, not shown, which engages or disengages the hydraulic piston. The preconcentrator control unit 214 is a stepper motor which rotates the filter elements 206 and 208 after they are no longer locked in place by the hydraulic control unit 210a.
The stepper motor is run under soft~are control. The interface control unit 238 is also a stepper motor, and it is used to rotate the multi-port valve 226, used in the sëcondary preconcentrator 203, from position 1 to position 2 and vise versa. Data from the analyzers 234 and 236 is brought directly into the computer 302 for processing. Data from the gas chromatograph/ECD system 234 is taken into the computer 302 as a varying frequency, and data from the IMS
3 system 236 is taken into the computer 302 as a varying analog voltage. The data input to the computer 302 is correlated by -36- ~32~9~ -processor 302 to the process control module 308 which generateS the necessary inte~rupts for processor 302 so the data can be input at the proper time intervals.
The computer 302 has an internal clock ~hich provides the reference clock for all timing se~uences.
Therefore, because all the valves and mechanical motions are -~
being actuated by the computer, all gas and sample flows in the equipment are controllable with respect to the time of actuation. The re ative sequencing and timing of actuations are simply steps in a stored program in the memory of the computer. In addition, all the temperatures in the equipment are read into the computer and all heating functions are actuated by the computer. Therefore, all the temperatures and their magnitudes at any time and rate of change with respect to time are under program control. The data output from the ECD 234 and the Il~1S 236 are processed as necessary and the required information is extracted and displayed by the same computer.
Figure 13 is a flow chart 400 showing the overall process control as accomplished by the control and data processing systems and run by the computer 302. ~lock 402 of flow cAart 400 is simply the starting point or entry into the entire soft~are package. The Run Diagnostics block 404 represents the block of software that is responsible for self diagnostics and self calibration. The Sample Air block 406 represents the block of code that causes the air sample drawn from the sampling port of the sampling chamber to be drawn into the SCAP. The Release Filters block 408 represents the block of software that is responsible for the control of the hydraulic control unit. The Rotate Filters block 410 - ~--3 represents the block of software responsible for the control of the preconcentrator control unit. The Lock Filters block 412 represents the block of software that is responsible for 132g~

the control of the hydraulic control unit in that it commands l the unit to lock the filter elements in the holding means.
The Desorb Va~or bloc~ 414 represents the block of soft~are that is responsible for the controlling of the heating means and the flow of pure gas in the desorption process. The Rotate ~lultiport Valve block 416 represents the block of soft~are that is responsible for controlling the multiport valve of the secondary preconcentrator so that the concentrated sample is properly routed to the analyzers. The Acquire Data block 418 represents the block of software that is responsible for the acquisition of data from the analyzers and the subsequent analysis and display of the resultant data. The software is a cyclic process and following step 418, returns to sampling ste~ 406 and continues until stopped. As stated previously, the software routine is modularized and therefore can be easily changed, updated, removed or added on to.
There are t~o schemes that exist for the screening process. The sequential scheme requires approximately 14.0 seconds to complete one screening cycle and the concurrent scheme requires approximately 3.6 seconds to complete one screening cycle. Both schemes are implemented using the flow chart 400 illustrated in Figure 13; however, as the name implies, the concurrent scheme involves performing certain of the operations involved in the screening process in an overlapping or multi-tasking environment. Basically, in the concurrent scheme, the software routines are run in a foreground/background scenario in a true interrupt mode. In - this type of scenario the mechanical operations can be run in background while the analysis and data processing can be run 3 in foreground. Figure 13 is a general representation of the software and should not be construed as a timing diagram.
Ta~le 1 given below illustrates the required steps and associated times involved in the screening procedure utilizing the sequential scheme. -' ~ _3~_ 1 32~4~

1 SA~PLE COLL~CTION 5.0 seconds PRI~RY CONC~NTRATION STAGE 3.0 seconds SECOND~RY CONCE~TR~TION STAGE 2.0 seconds 5 AN~LysIs 3.0 seconds DATA PROCESSING/REPORTI~IG 1.0 seconds TOTAL SCREEI~ING TI~lE 14.0 seconds Table 1 Referring now to Figure 14, a se~uence diagram 500 or timing chart is given in order to illustrate the various -time parameters for each given in the concurrent sampling scheme. Each time bar is comprised of five boxes indicating the various steps in the process. Box 502 represents the air sampling step time, box 504 represents the time for the mechanical steps involved in the collection of the sample, box 506 represents the time associated for injecting the concentrated sample into the chemical analyzers, and box 510 represents the analysis time. Since it takes approximately 2.5 seconds to pass through the portal, two people can pass through in 5.0 seconds, and thus the timing chart 500 is shown for two people. To calculate the total time for a single person; which is approximately 3.6 seconds, the total time for the first two people to be screened, which is 14.4 seconds, has subtracted from it the time for sampling and ~ - -collecting the sample from the next two people, which is approximately 7.2 seconds, resulting in a time of ~
approximately 7.2 seconds for two people and 3.6 seconds for - ~-30 a single person. As indicated in chart 500, the concurrent -scheme overlaps in the sampling and collection periods. The three remaining time lines are identical numerals with -: .. ', .. .
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_39- ~32~

prime, double prime and triple primes added. It is important 1 to note that if an alarm indicating a particular substrate does go off, it is necessary to send the two people thxouqh individually, thus ta~;ing appro~imately 14.0 seconds as indicated in the previous paragraph.
Although shown and described in what is believed to be the most practical and preferred embodiments, it is apparent that departures from specific methods and designs described and shown will suggest themselves to those skilled in the art and may be used without departing from the spirit and scope of the invention. The present invention is not restricted to the pariicular constructions described and illustrated, but should be constructed to cohere of all modifications that may fall within the scope of the appended claims`
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Claims (55)

1. A walk-through explosive detection screening system for the detection of concealled explosives, chemical agents and other controlled substances such as drugs or narcotics by detecting their vapor or particulate emissions, said system comprising:
(a) a walk-through sampling chamber means for gathering a sample of the environment surrounding a person or object passing through said sampling chamber means by sweeping the vapor or particulate emissions from said person or object, said sampling chamber means having an entrance and exit portal defined by at least two walls, and a convergent ceiling which opens into an air plenum;
(b) a pair of inwardly directed and vertically oriented air flow guide means on either side of each of said entrance and exit portals, said air flow guide means directing air towards a center region of said sampling chamber means with a predetermined velocity, the combination of said air flows from said pair of inwardly directed and vertically oriented air flow guide means creating a dynamic high pressure zone in said sampling chamber means;
(c) means for recirculating air between said pair of inwardly directed and vertically oriented guide means and said air plenum, the recirculating air creating a dynamic low pressure zone in the region of said convergent ceiling, said dynamic high and low pressure zones creating a region within said sampling chamber means that does not allow an appreciable amount of air in or out of said entrance and exit portals;
(d) a sample collection means to collect a sample volume of air that is swept off the individual or object passing through said sampling chamber means, said sample collection means including means for collecting a volume of air from a sampling port mounted in the plenum and centered in said convergent ceiling;
(e) means for concentrating said vapor or particulate emissions collected by said sample collection means, said means for concentrating having a first means for adsorption and a second means for desorption of said concentrated vapor or particulates;
(f) detecting means responsive to said vapor or particulate emissions desorbed from said second means for desorption to generate a first signal and an alarm.

2. The walk-through explosive detection screening system of Claim 1 wherein said walk-through sampling chamber means has a rectangular geometry approximately six feet in length, three feet in width and seven feet in height, said walk-through sampling chamber means having a conically shaped ceiling.

3. The walk-through explosive detection screening system of Claim 2 wherein said pair of inwardly directed and vertically oriented air flow guide means are six slots of one foot in length and a half inch in width in a pair of six inch diameter end columns mounted on either side of each of said entrance and exit portals, said end columns having inch and a half internal guide vanes to form exiting air into a first jet stream.

4. The walk-through explosive detection screening system of Claim 3 wherein said six slots are at an angle of 45 degrees pointing towards the center of said walk-through sampling chamber means.

5. The walk-through explosive detection screening system of Claim 3 wherein said first jet stream has a velocity of approximately 17 meters per second.

6. The walk-through explosive detection screening system of Claim 5 wherein said walk-through sampling chamber means further comprises a pair of side air flow pipes, said pair of side air flow pipes run along said floor and are connected to each of said pair of six inch diameter end columns.

7. The walk-through explosive detection screening system of Claim 6 wherein said pair of side air flow pipes each contain a twelve inch long by half inch wide air slot in the center of each of said pair of side air flow pipes, said air slots forming exiting air into a second jet stream.

8. The walk-through explosive detection screening system of Claim 7 wherein said air slots are at an angle of 45 degrees pointing upwards to the center of said walk-through sampling chamber means.

9. The walk-through explosive detection screening system of Claim 8 wherein said second jet stream has a velocity of approximately 15 meters per second.

10. The walk-through explosive detection screening system of Claim 7 wherein said means for recirculating air comprises a plurality of fans connected on a suction end to said plenum and on a discharge end to said pair of six inch diameter end column.

11. The walk-through explosive detection screening system of Claim 10 wherein said plurality of fans are each capable of delivering 1000 cubic feet of air per minute.

12. The walk-through explosive detection screening system of Claim 1 wherein said sampling port is centered in a collection duct having a rectangular geometry with dimensions of 16 inches by 20 inches by 6 inches.

13. The walk-through explosive detection screening system of Claim 11 wherein said sample collection means further includes a transportation means for collecting said volume of air from said sampling port and transporting said volume of air to said concentrating means.

14. The walk-through explosive detection screening system of Claim 13 wherein said transportation means is a pipe with a first end open as said sampling port and a second end connected to a suction fan for drawing said volume of air from said sampling port at predetermined times, said pipe can be stainless steel, aluminum or ABS plastic.

15. The walk-through explosive detection screening system of Claim 14 wherein said concentrating means comprises a primary preconcentrator.

16. The walk-through explosive detection screening system of Claim 15 wherein said first means for adsorption and said second means for desorption are first and second filter means mounted on a movable platform.

17. The walk-through explosive detection screening system of Claim 16 wherein said first and second filter means are movable between an adsorption position and a desorption position, each of said filter means being in line with said suction fan and operable to adsorb vapor and/or particulate emissions contained in said volume of air in said adsorption position, and each of said filter means being in line with an interface means when said adsorbed vapor and/or particulate emissions are desorbed.

18. The walk-through explosive detection screening system of Claim 17 wherein said primary preconcentrator further comprises a third filter means mounted on said movable platform between said first and second filter means.

19. The walk-through explosive detection screening system of Claim 18 wherein said first, second and third filter means are movable between said adsorption position, said desorption position, and a thermal cleaning position, each of said filter means being in line with said suction fan and operable to adsorb vapor and/or particulate emissions contained in said volume of air in said adsorption position, each of said filter means being in line with an interface means when said adsorbed vapor and/or particulate emissions are desorbed, and each of said filter means being in line with a thermal cleaning means when other filter means are being adsorbed and desorbed.

20. The walk-through explosive detection screening system of Claim 19 wherein said primary preconcentrator comprises a gas supply means for supplying a clean gas flow to said first, second and third filter means when said respective filter means is in said desorption position, and in said thermal cleaning position said clean gas flow is used to desorb and sweep said concentrated vapor and/or vapor emanating from particulate matter into said interface means when said filter means is in said desorption position, and said clean gas flow is used to thermally clean and sweep residue into the ambient environment.

21. The walk-through explosive detection screening system of Claim 20 wherein said clean gas is an inert gas.

22. The walk-through explosive detection screening system of Claim 21 wherein said first, second and third filter means comprise wire screens which hold a selected adsorbing material coated thereon.

23. The walk-through explosive detection screening system of Claim 22 wherein said primary preconcentrator still further comprises a heat exchanger for supplying heat to each of said filter means when they are in said desorption and said thermal cleaning position to aid in desorbing the vapor and/or particulate emissions.

24. The walk-through explosive detection screening system of Claim 20 wherein both said first, second and third filtering means are each movable between said adsorption position, said desorption position, and said thermal cleaning position, said second filter means occupying said desorption position when said first filter means occupying said adsorption position and when said third filter means occupying said thermal cleaning position, and said third filter means occupies said adsorption position when said first filter means occupies said desorption position and said second filter means occupying said thermal cleaning position.

25. The walk-through explosive detection screening system of Claim 20 wherein said first, second and third filter means are moved by a control system.

26. The walk-through explosive detection screening system of Claim 25 wherein said control system comprises:
a hydraulic control unit and pump connected to said platform by a rigid shaft, said hydraulic control unit is operable to move said platform from a locked position to an unlocked position; and a preconcentrator control unit which is operable to rotate said platform when said platform is in the unlocked position.

27. The walk-through explosive detection screening system of Claim 26 wherein said preconcentrator control unit is a stepper motor.

28. The walk-through explosive detection screening system of Claim 20 wherein said interface means is a connector tube which connects said primary preconcentrator to said detection means and which carries said concentrated vapor and/or vapors emanating from particulate matter from said primary preconcentrator to said detection means.

29. The walk-through explosive detection screening system of Claim 20 wherein said interface means is a secondary preconcentrator which comprises a multi-port valve system.

30. The walk-through explosive detection screening system of Claim 29 wherein said multi-port valve system comprises a six-port valve which contains an adsorption/desorption tube connected across two of said six-ports and four gas lines, said six-port valve being rotatable between an adsorb position and an desorb position.

31. The walk-through explosive detection screening system of Claim 30 wherein said six-port valve is rotated by an electronic interface control unit.

32. The walk-through explosive detection screening system of Claim 31 wherein said interface control unit includes a stepper motor.

33. The walk-through explosive detection screening system of Claim 30 wherein the six-port valve is in said adsorb position when said concentrated vapor and/or vapor emanating from particulate matter is passed through said adsorption tube for further concentration.

34. The walk-through explosive detection screening system of Claim 30 wherein the six-port valve is in said desorb position when said further concentrated vapor and/or vapor emanatting from particulate matter is desorbed and swept into said detection means.

35. The walk-through explosive detection screening system of Claim 30 wherein said adsorption/desorption tube further includes a thermocouple or thermistor for monitoring the desorption temperature of the tube.

36. The walk-through explosive detection screening system of Claim 30 wherein said adsorption/desorption tube is electrically connected to a controlled current source which is used to heat the tube to a predetermined temperature as part of the desorption process.

37. The walk-through explosive detection screening system of Claim 34 wherein said interface means further comprises a gas supply means for sweeping said further concentrated vapor and/or vapors emanatting from particulate matter into said detection means.

38. The walk-through explosive detection screening system of Claim 37 wherein said detection means comprising an ion mobility spectrometer (IMS) for analyzing said further concentrated vapor and/or vapors emanatting from particulate matter and generating said first signal if a target material is detected.

39. The walk-through explosive detection screening system of Claim 37 wherein said detection means comprises an gas chromatograph/electron capture detector for analyzing said further concentrated vapor and/or vapors emanatting from particulate matter and generating said first signal if a target material is detected.

40. The walk-through explosive detection screening system of Claim 37 wherein said detection means comprises a photo ionization detector.

41. The walk-through explosive detection screening system of Claim 37 wherein said detection means comprising a nitrogen phosphorous detector.

42. The walk-through explosive detection screening system of Claim 37 wherein said detecting means comprises an ion mobility spectrometer and a gas chromatograph/electron capture detector for analyzing said further concentrated vapor and/or vapor emanatting from particulate matter and generating said first signal if a target material is detected.

43. The walk-through explosive detection screening system of Claim 42 wherein said system further includes a control and data processing means which further comprises:
a digital computer with a stored digital program which is responsible for the control of the system; and a process control module which is an interface between said digital computer and said interface control unit, said preconcentrator control unit and said control unit.

44. The walk-through explosive detection screening system of Claim 43 wherein said stored digital program is operable to control a plurality of processes including said self diagnostic and self calibration processes, control of said sample collection, and processing of collected data from said detection means.

45. A method for the detection of concealled explosive chemical agents and other controlled substances such as drugs or narcotics by detecting their vapor or particulate emissions, said method comprising the steps of:
(a) gathering a sample of the environment surrounding a person or object passing through a sampling chamber by sweeping the vapor or particulate emissions from said person or object;
(b) directing air towards a center region of said sampling chamber means with a predetermined velocity from a pair of inwardly directed and vertically oriented air flow guide means in order to create a dynamic high pressure zone in said sampling chamber, said dynamic high pressure zone creating a region within said sampling chamber that does not allow an appreciable amount of air in or out of an entrance and exit portal of said sampling chamber means;
(c) recirculating air between said pair of inwardly directed and vertically oriented guide means and an air plenum, the recirculating air creating a dynamic low pressure zone in the region of a convergent ceiling in said sampling chamber means;
(d) collecting a sample volume of air that is swept off the individual or object passing through a said sampling chamber means, said sample collection means including means for collecting a volume of air from a sampling port mounted in the plenum and centrally located in said convergent ceiling;
(e) concentrating said vapor or particulate emissions collected by said sample collection means, said means for concentrating having a first means for adsorption and a second means for desorption of said concentrated vapor or vapors emanatting particulate emissions;
(f) detecting said vapor or particulate emissions desorbed from said second means for desorption.

46. The method for the detection of concealled explosives according to Claim 45 wherein said directing air includes forming exiting air into a first jet stream at an angle of 45 degrees pointing towards the center of said sampling chamber means with a velocity of approximately 17 meters per second.

47. The method for the detection of concealled explosives according to Claim 46 wherein said directing air step further includes forming air exiting from a pair of side air flow pipes into a second jet stream at an angle of 45 degrees pointing upwards towards the center of said sampling chamber means with a velocity of approximately 15 meters per second.

48. The method for the detection of concealled explosives according to Claim 47 wherein said collecting step further comprises transporting said volume of air to said concentrating means.

49. The method for the detection of concealled explosives according to Claim 48 wherein said concentrating step comprises adsorbing target materials in a first position and desorbing target materials in a second position.

50. The method for the detection of concealled explosives according to Claim 49 wherein said desorbing target materials in a second position comprises the steps of:
heating said target materials to a predetermined desorbing temperature or a predetermined vaporing temperature; and sweeping said target materials with an inert gas.

51. The method for the detection of concealled explosives according to Claim 50 wherein said step of detecting includes sweeping said target materials and inert gas into a detection means.

52. The method for the detection of concealled explosives according to Claim 51 wherein said step of detecting further includes chemically analyzing said target materials.

53. The method for the detection of concealled explosives according to Claim 52 which further includes the step of controlling the collection and processing of data with a digital computer which utilizes a stored program.

54. The method for the detection of concealled explosives according to Claim 48 wherein said concentrating step further comprises thermally cleaning the residue from a third means for adsorption and desorption when said third means is in a thermally cleaning position.

55. The method for the detection of concealled explosives according to Claim 54 wherein said thermally cleaning comprises the steps of:
heating said residue on said third means to a predetermined temperature; and sweeping said heated residue to the ambient environment.