Method and apparatus for temperature controlled samplers

Claim 2

In a method of measuring the amount of one gas in another gas using bubblers and reagents each responsive to a particular gas in which the temperature of one reagent is controlled to be within a predetermined temperature range, the improvements in controlling the temperature of said one reagent comprising the steps of establishing a first ambient temperature zone, establishing a second temperature zone containing the bubblers and reagents, establishing a third controlled temperature zone within said second zone containing said one of said reagents, and using said first zone as a heat sump for said third zone independently of said second zone.

Claim 3

The method of claim 1, and maintaining relatively constant pressure throughout the system.

Claim 4

The method of claim 1, and heating said second zone.

Claim 5

The method of claim 1, wherein said temperature range is selected so as to not degrade the one gas to which said particular reagent is responsive.

Claim 6

The method of claim 1, wherein said particular reagent is responsive to SO 2 .

Claim 7

The method of claim 1, and controlling said third zone temperature with a thermo-electric heating/cooling means and bracketing thermostats in heat exchange relationship with said one reagent.

Claim 8

In a bubbler type gas sampler comprising a plurality of reagent tubes in parallel each containing a reagent responsive to a selected one of various components in sample gas flowed through the system, the combination comprising pump means for moving sample gas through all of the tubes in parallel, means to maintain a relatively constant pressure throughout the system, said sampler being contained in a cabinet, means to establish a first temperature zone in said cabinet communicating with the ambient atmosphere, a second temperature zone in said cabinet defined by insulation means and surrounding all of said reagent tubes, and a third temperature zone within said second temperature zone comprising a selected one of said reagent tubes, means to control the temperature of said selected one reagent tube within said third zone, means to heat said second zone, said temperature control means for said third zone extending through said second zone and into said first zone, whereby said first zone acts as a heat sump for the heat to be pumped into or out of said third zone, whereby said first and third zones are in heat flow communication with each other, and whereby said second zone is insulated from both said first and third zones.

Claim 9

In a bubbler type gas sampler comprising a plurality of reagent tubes in parallel each containing a reagent responsive to a selected one of various components in sample gas flowed through the system, the combination comprising pump means for moving sample gas through all of the tubes in parallel, means to maintain a relatively constant pressure throughout the system, said sampler being contained in a cabinet, means to establish a first temperature zone in said cabinet communicating with the ambient atmosphere, a second temperature zone in said cabinet defined by insulation means and surrounding all of said reagent tubes, and a third temperature zone within said second temperature zone comprising a selected one of said reagent tubes, means to control the temperature of said selected one reagent tube within said third zone, means to heat said second zone, said temperature control means for said third zone extending through said second zone and into said first zone, whereby said first zone acts as a heat sump for the heat to be pumped into or out of said third zone, whereby said first and third zones are in heat flow communication with each other, and whereby said second zone is insulated from both said first and third zones.

Claim 10

The combination of claim 7, and means to heat said second zone.

Claim 11

The combination of claim 7, and temperature sensing means comprising first and second thermostats in heat exchange relationship with said reagent tube, and said thermostats operating at different predetermined temperatures to thereby define a predetermined temperature range within which the temperature of said reagent tube will be held.

Claim 12

The combination of claim 1, said temperature control means comprising thermo-electric heating/cooling means in a heat exchange relationship with said selected reagent tube, means to sense the temperature of said reagent tube, control means interposed between said temperature sensor means and said thermo-electric heating/cooling means, said temperature sensor means operating said thermo-electric heating/cooling means via said control means so as to maintain the temperature of said reagent tube within a predetermined temperature range.

Claim 13

The combination of claim 9, wherein said thermo-electric heating/cooling means comprises a plurality of fins extending from a block and a thermo-electric member on said block on the side thereof opposite said fins, said thermo-electric member being in said third zone and said fins being in said first zone, means to flow air across said fins, whereby said fins serve to remove heat from the first zone ambient air and to supply said heat to said thermo-electric member when said thermo-electric heating/cooling means is in a heating mode, and wherein said fins serve to put heat into the air flowing thereover when said thermo-electric member is in a cooling mode.

Claim 14

The combination of claim 7, wherein said selected gas is SO 2 , said temperature control means comprising thermo-electric heating/cooling means in heat exchange relation with said selected tube in said third zone and with said first zone, D.C. power supply means, and means to connect said D.C. power supply means to said thermo-electric heating/cooling means in either a heating or cooling relation thereto in order to maintain the temperature in a predetermined range.

Claim 15

The combination of claim 12, said last mentioned means comprising a pair of bracketing thermostats adapted to sense the temperature of said selected reagent tube, said means further comprising control means including a plurality of relays interconnected between said D.C. power supply means and said thermo-electric heating/cooling means, said plurality of relays being operated by said bracketing thermostats to achieve said aforementioned mode of operation.

Claim 16

The combination of claim 7, and trap means associated with each of said reagent tubes, an inlet manifold to supply sample gas to all of said reagent tubes, an outlet manifold connected to all of said trap means, crossover means from each of said reagent tubes to its associated trap means, a rack mounting all of said tubes, trap means, manifolds and crossover means on said rack, whereby all of said tubes, trap means, manifolds and crossover tubes may be removed from said sampler second zone by simply disconnecting the inlet and outlet means to said inlet and outlet manifolds respectively, whereby cleaning, maintenance and the like of the sample handling portions of the sampler are facilitated.

Claim 17

The combination of claim 14, wherein first mentioned selected component is SO 2 and wherein all of said tubes and other portions of the tubes, trap means, manifolds and other portions of said apparatus which come into contact with the sample gas are made of glass and other materials which have no effect upon SO 2 .

Claim 18

The combination of claim 7, and means to maintain a relatively constant pressure throughout the system.

Claim 19

The combination of claim 16, said sampler including pump means for drawing sample gas through all of said liquid reagent filled tubes, and said constant pressure means comprising critical flow means operatively cooperative with said pump means and said bubbler.

Claim 20

The combination of claim 17, said critical flow means comprising a hypodermic syringe needle having a predetermined inside diameter.

Claim 21

The combination of claim 17, said critical flow means comprising a glass orifice of a predetermined inside diameter.

Claim 22

In a bubbler gas sampler of the type wherein sample gas is flowed through a liquid reagent responsive to a selected component in the sample gas, the improvement comprising thermo-electric heating/cooling means in heat exchange relationship with said reagent, means to sense the temperature of said reagent, control circuit means interposed between said temperature sensor means and said thermo-electric heating/cooling means, said temperature sensor means operating said thermo-electric heating/cooling means via said control circuit means so as to maintain the temperature of said reagent within a predetermined temperature range, and heat sump means in heat exchange relationship with said thermo-electric heating/cooling means.

Claim 23

In a bubbler gas sampler of the type wherein sample gas is flowed through a liquid reagent responsive to a selected component in the sample gas, the improvement comprising thermo-electric heating/cooling means in heat exchange relationship with said reagent, means to sense the temperature of said reagent, control circuit means interposed between said temperature sensor means and said thermo-electric heating/cooling means, said temperature sensor means operating said thermo-electric heating/cooling means via said control circuit means so as to maintain the temperature of said reagent within a predetermined temperature range, and heat sump means in heat exchange relationship with said thermo-electric heating/cooling means.

Claim 24

The combination of claim 20, said temperature sensing means comprising first and second thermostats in heat exchange relationship with said reagent, and said thermostats operating at different predetermined temperatures, whereby the temperature difference between said predetermined temperatures determines said predetermined temperature range within which the temperature of said tube will be held.

Claim 25

The combination of claim 20, wherein said selected component is SO 2 , said control means comprising a pair of bracketing thermostats adapted to sense the temperature of said selected reagent, D.C. power supply means, and a plurality of relays interconnected between said D.C. power supply means and said thermo-electric heating/cooling means, and said plurality of relays being operated by said bracketing thermostats to achieve said aforementioned mode of operation.

Claim 26

The combination of claim 20, wherein said heat sump means comprises a plurality of fins extending from a block, said thermo-electric heating/cooling means comprising a thermo-electric member on said block on the side thereof opposite said fins, means to flow air across said fins, whereby said fins serve to remove heat from the ambient air and so supply said heat to said thermo-electric member when said thermo-electric heating/cooling means is in a heating mode, and wherein said fins serve to put heat into said ambient air flowing thereover when said thermo-electric member is in a cooling mode.

Claim 27

The combination of claim 23, said air flow means operating constantly whenever said sampler is on, pump means for flowing said sample gas so arranged that said air flows across said fins and said pump means.

Claim 28

The combination of claim 20, said sampler including pump means for drawing sample gas through at least one of said liquid reagent filled tubes, and critical flow means operatively cooperative with said pump means and said bubbler.

Claim 29

The combination of claim 25, said critical flow means comprising a hypodermic syringe needle having predetermined inside diameter.

Claim 30

The combination of claim 25, said critical flow means comprising a glass orifice of a predetermined diameter.

Claim 31

The combination of claim 20, wherein said sampler comprises a plurality of said tubes each containing a different liquid reagent responsive to a different selected component in the sample gas, each of said reagent tubes being associated with a trap tube, an inlet manifold to supply sample gas to all of said reagent tubes, an outlet manifold connected to all of said reagent tubes, an outlet manifold connected to all of said trap tubes, crossover means from each of said reagent tubes to its associated trap tube, a rack, means to mount all of said tubes and manifolds and crossover means on said rack, whereby all of said tubes, manifolds and crossover tubes may be removed from said sampler by simply disconnecting the inlet and outlet means to said inlet and outlet manifolds respectively, whereby cleaning, maintenance and the like of the sample handling portions of the sampler are facilitated.

Claim 32

The combination of claim 28, said sampler including pump means for drawing sample gas through all of said liquid reagent filled tubes, and critical flow means operatively cooperative with said pump means and said bubbler.

Claim 33

The combination of claim 28, wherein said first mentioned selected component is SO 2 and wherein all of said tubes and other portions of the tubes, manifolds and other portions of said apparatus which come into contact with the sample gas are made of glass and other materials which have no effect upon SO 2 .

Claim 34

In combination, a bubbler type gas sampler comprising a plurality of reagent tubes in parallel each containing a reagent responsive to a selected component in sample gas bubbled through the tube, means for moving said sample gas through said tubes in parallel, critical flow means in the sample flow stream for maintaining a relatively constant sample gas pressure through the system regardless of pressure fluctuations in the system, and means to maintain the temperature of at least one said reagents within a predetermined temperature range.

Claim 35

In combination, a bubbler type gas sampler comprising a plurality of reagent tubes in parallel each containing a reagent responsive to a selected component in sample gas bubbled through the tube, means for moving said sample gas through said tubes in parallel, critical flow means in the sample flow stream for maintaining a relatively constant sample gas pressure through the system regardless of pressure fluctuations in the system, and means to maintain the temperature of at least one said reagents within a predetermined temperature range.

Claim 36

The combination of claim 31, wherein each of said reagent tubes is associated with a trap tube, an inlet manifold to supply sample gas to all of said reagent tubes, an outlet manifold connected to all of said trap tubes, crossover means from each of said reagent tubes to its associated trap tube, a rack carrying all of said tubes, manifolds and crossover means, whereby all of said tubes, manifolds and crossover tubes may be removed from said sampler by simply disconnecting the inlet and outlet means to said inlet and outlet manifolds respectively, whereby cleaning, maintenance and the like of the sample handling portions of the sampler are facilitated.

Claim 37

The combination of claim 32, wherein said selected reagent is responsive to SO 2 and wherein all of said tubes and other portions of the tubes, manifolds and other portions of said apparatus which come into contact with the sample gas are made of glass and other materials which have no effect upon SO 2 .

Claim 38

The combination of claim 31, said sampler including pump means for drawing sample gas through all of said liquid reagent filled tubes, and critical flow means operatively cooperative with said pump means and said bubbler.

Claim 39

The combination of claim 34, said critical flow means comprising a glass orifice of a predetermined capillary-like diameter.

Claim 40

The combination of claim 34, said critical flow means comprising a hypodermic syringe needle having a predetermined inside diameter.

Claim 41

The combination of claim 31, said temperature control means cmprising thermo-electric heating/cooling means in heat exchange relation with said selected reagent tube, D.C. power supply means, and means to connect said D.C. power supply means to said thermo-electric heating/cooling means in either a heating or cooling relation thereto as required in order to maintain said temperature in said predetermined range.

Claim 42

The combination of claim 37, said last mentioned means comprising a pair of bracketing thermostats adapted to sense the temperature of said selected reagent tube, said means further comprising control means including a plurality of relays interconnected between said D.C. power supply means and said thermo-electric heating/cooling means, said plurality of relays being operated by said bracketing thermostats to achieve said aforementioned mode of operation.

Claim 43

The combination of claim 37, and heat sump means in heat exchange relationship with said thermo-electric heating/cooling means, said heat sump means comprising a plurality of fins extending form a block, said thermo-electric heating/cooling means comprising a thermo-electric member on said block on the side thereof opposite said fins, means to flow air across said fins, whereby said fins serve to remove heat from the ambient air and to supply said heat to said thermo-electric member when said thermo-electric heating/cooling means is in a heating mode, and wherein said fins serve to put heat into said ambient air flowing thereover when said thermo-electric member is in a cooling mode.

Claim 44

The combination of claim 39, said air flow means operating constantly whenever said sampler is on, pump means creating said sample flow, and said air flow also cooling said pump means.

Claim 47

The method of claim 41, wherein said selected gas of interest is SO 2 , and wherein said predetermined temperature is selected to prevent degradation of SO 2 .

Claim 48

The method of claim 41, and the step of vacuum drawing sample gas through all of said liquid reagent filled tubes.

Claim 49

The method of claim 41, said temperature maintenance means comprising a thermo-electric heating/cooling means, and the steps of putting the operative portion of said thermo-electric heating/cooling means in heat flow communication with said tube and putting heat flow fins for said thermo-electric heating/cooling operative portion in a forced air heat sump.

Claim 50

The method of claim 41, and operating said forced air heat sump constantly, and putting the pump means which flows the gas through the system in the path of said forced air to cool said pump means.

Claim 51

The method of claim 41, wherein said reagent is responsive to SO 2 .