HENSI Immobilization Demonstration Videos Page
Now with Streaming Video (video #1) !
Video # 1 - New 'C' Series HENSI R&D-Size Systems (like those shown
below) in Action Immobilizing ZVI / Palladium Nano-catalyst !
Please Excuse Us - PID's Being Updated
Notes About Video # 3 Link Below)

  • Video 2 is 16 minutes long and shows the 2nd
    Prototype HENSI Reactor immobilizing Golder &
    Associates Iron/Palladium nano-catalyst for
    subsequent on-line, flow-through uses in any
    catalytic scenario.  This catalyst was chosen
    because it is especially effective for in the rapid
    breakdown of any of ~39 recalcitrant chlorinated
    hydrocarbon water pollutants ubiquitous to our
    (often otherwise potable) groundwaters.  As
    such, when HENSI - immobilized on a large scale,
    Fe/Pd nanocatalysts could be quite effective for
    ex-situ, high-throughput, Point-Of-Distribution, on-
    demand remediation-to-potable-quality of
    hundreds of US aquifers.
  • For initial loading into the HENSI reactor, the
    nanocatalysts are added to 1 gal water (in a
    sump bucket), which is then circulated through
    the HENSI reactor and back into the bucket at
    ~1GPM
  • As the HENSI reactor is energized, the
    nanocatalysts (in solution) being pumped through
    it are immediately immobilized in the unit
    (removed from solution and captured in an
    homogeneous distribution within the reactor), as
    evidenced by the HENSI discharge stream
    immediately becoming clear
  • In the experiment, in order to keep the system
    volume at 1 gallon (no water source or drain was
    available) the clear discharge is sent back into
    the sump bucket, and mixed with the turbid
    nanocatalysts solution
  • Therefore the solution in the bucket slowly
    clarifies, asymptotically reaching the clarity of the
    discharge stream, but note that the discharge
    stream remains clear throughout the capture
    process
  • Once the bucket has reached a clarity under
    about 1 NTU (about 3 minutes) the reactor is fully
    charged, The system would be put into normal
    operation: the (polluted) process fluid would them
    be routed through the reactor, exposing it to the
    immobilized nanocatalyst to achieve the desired
    breakdown of carcinogens to benign species -
    online remediation, often to potable quality water
    in this one unit operation.
  • The video, however, continues with the de-
    energizing of the HENSI unit to release the
    nanocatalysts from their immobilized state, back
    into the flowing solution.  This is done only to
    demonstrate the reversibility of the process:  In
    actual practice, this step would only be carried
    out after the catalyst was spent, or for catalyst
    regeneration / recharge operations. The video
    then repeats the entire process of capture and
    release, just for good measure.  The second
    time, however, I actually route the reactor
    discharge into a clear plastic container, that the
    viewer might see that the reactor discharge
    stream is unmistakably free of nano-catalyst,
    indicating that the immobilization is thorough and
    complete
  • It is important to note that I have yet to approach
    the actual capacity for this (yet-to-be-optimized)
    HENSI unit:  In the first video I immobilize 20
    grams of nanocatalyst within the HENSI reactor.  
    In the second video I immobilize approximately
    100 grams in the same reactor, for a 'Loading
    Density' of [100 g catalyst x 30 m2/gram / 14in3
    =~ 200 square meters of catalytic surface
    area per cubic inch of reactor volume, and
    much greater 'loading densities' may well be
    attainable once the systems are optimized.
  • The important point is that the combination
    of this density of catalytic area per unit
    reactor volume (with all the catalytic surface
    area exposed to the bulk reactant), the
    complete and thorough nature,and
    reversibility of the immobilization at low
    pressure drop, complete scalability and
    modularity,  and the low capital and
    operating costs will allow HENSI to truly
    usher in a new era in nano-catalysis for any
    application which can benefit from ex-situ
    processing.
Notes About Video # 2 (Link Below)

  • Video 1 is only about 8.5 minutes long.  It shows
    the 2nd Prototype HENSI Reactor immobilizing
    approximately 100 grams of Golder & Associates
    Iron/Palladium nano-catalyst for subsequent on-
    line, flow-through uses in any catalytic scenario.  
  • This video uses 2 gallons of water as the 'loading
    solvent' to mitigate any concentrations effects
    during loading
  • Video 1 has several differences from video #2,
    besides shorter duration (and file size):
  • It uses a clear feed 'bucket' and
    incorporates a clear discharge 'bucket' for
    visibility of the turbid 'loading' solution and
    the clear discharge solution
  • It incorporates a Hach OptiQuant
    Suspended Solids Meter with an in-situ
    sensor to give an objective readout of the
    Total Suspended Solids in the HENSI feed
    and discharge solutions during catalyst
    loading:  This meter indicates objectively
    that the total suspended solids in the HENSI
    discharge water stream are LESS than that
    of the tap water into which the 100 grams of
    nanoparticles are poured prior to initiating
    the loading cycle
  • It was filmed with a different camera, with
    less light, and at much lower resolution in
    order to decrease file size.  Hence, it is
    more difficult to see the smaller details in
    this video.  Most importantly, it is difficult to
    see the readout value on the Hach
    Suspended Solids Meter during the run.  
    For this reason, as you are playing the
    video, please PAUSE THE VIDEO AT THE
    FOLLOWING POINTS IN PLAY-TIME:
  • 3:30 (3 min. 30 sec.) - TSS in
    'loading solution' (water in feed
    bucket) prior to the addition of the
    nano-catalyst particles - value is 69
    mg/l TSS
  • 4:46 (4 min. 46 sec.) - TSS in Feed
    Bucket after the addition of the
    nanocatalyst particles - value is
    ~4400 mg/l TSS
  • 8:25 (8min. 25 sec.) - TSS in
    discharge bucket just as the meter
    begins to read the discharge value -
    value is 33 mg/l TSS
  • 8:42.7 (8 min. 42.7 sec.) - TSS in
    discharge bucket as the meter
    reading stabilizes on the TSS in the
    discharge - value is 24 mg/l TSS
  • As the HENSI reactor is de-energized, the
    nanocatalysts (in solution) being pumped through
    it are immediately immobilized in the unit (removed
    from solution and captured in an homogeneous
    distribution within the reactor), as evidenced by
    the HENSI discharge stream immediately
    becoming clear
  • The video also includes the de-energizing of the
    HENSI unit to release the nanocatalysts from their
    immobilized state, back into the flowing solution.  
    Again, In this video I immobilize approximately 100
    grams of nanocatalyst, for a 'Loading Density' of
    [100 g x 30 m2/gram / 14in3 =~ 200 square
    meters of catalytic surface area per cubic
    inch of reactor volume.
  • The important point is that the combination
    of this density of catalytic area per unit
    reactor volume (with all the catalytic surface
    area exposed to the bulk reactant), the
    complete and thorough nature,and
    reversibility of the immobilization at low
    pressure drop, complete scalability and
    modularity,  and the low capital and operating
    costs will allow HENSI to truly usher in a new
    era in nano-catalysis for any application which
    can benefit from ex-situ processing.

HENSI Demo Video #1 (Std. file download)
Note: this 2nd link is to a ~8 minute,
~200 Megabyte .mpeg file, so the
download takes about 10 minutes even
with a high-speed connection.
PLEASE NOTE THAT THESE
VIDEOS MUST BE PAUSED
AT SEVERAL POINTS IN
ORDER TO CORRECTLY
VIEW THE VIDEO - SEE
NOTES ABOVE BEFORE
VIEWING!
HENSI Demo Video #2 Note: this
link is to a 16 minute, 367Megabyte
.mpeg file, so the download takes about
20 minutes even with a high-speed
connection - Have patience - it's worth
it