Our Company
•Purification and treatment of Breathable and
Industrial gases.
•Wide range of Transition & Precious Metal Oxidation
Catalysts
•Sliver Ion Exchange Zeolite
•Hydrogen getters
•Nano Hollow Fibre absorbents
•Suppliers of a wide range of Calcium Chloride
products
About Us
•Based in the UK Premier Chemicals are a customer focused
business in our core business areas, Calcium Chloride supply,
Gas Purification and Bio fuel raw material.
•We are committed to improving service standards to our
client partners through our knowledge of leading
technologies and our customer focus.
•The drive of this is to improve our service and to drive our
client partner’s profitability.
What We do
Oxidation Catalyst
•Transition Metal Catalyst
–Hopcalite
•Precious Metal Catalysts
–Nano Particulate Gold
–Supported Platinum
•Applications
•Carbon Monoxide Oxidation
•VOC Abatement
•Destruction of Ethylene Oxide & Ozone
•UHP Gas
Silver Ion Exchanged Zeolite
•Applications
–Hydrogen Getter in Cryogenic vessels and lines
–Hydrogen Getter in Optical fibre
–Removal of Radioactive Iodine
–Treatment of Iodine in Acetic Acid Manufacture.
Hydrogen Getters
Applications
•Absorption in battery compartments
•Absorption in packaging of Electronics
•Absorption in Optical fibre modules
•Absorption in Cryogenic vessels
Calcium Chloride
•Suppliers of Bulk Calcium Chloride
•Anhydrous to Di-hydrate
–Gas Drying
–De-icing
–Water Treatment
–Pharmaceutical additive
–Food additive
Nano Particulate Hollow fibre Technology
Premier Chemicals & N-psl
Delivering Innovation in Gas absorption
Mission
“To be pre-eminent in the
technology of nano-porous
composite hollow fibres and
to supply high added value
products and solutions to
customers world-wide”
Intellectual Property
Patent Summary
International Patent Application
No. PCT/GB2006/002509 entitled
“Hollow fibres”
Number of hollow fibre recipes for robust and
flexible nano-porous fibres, including a
method and apparatus for processing of
highly viscous dopes.
UK Patent Application
No. 07049349
Hollow fibre recipes, and adsorption units
based on the use of conductive fibres that can
be easily “regenerated”.
UK Patent Application
No. P402739
Advanced Compressed Air Treatment
Design
Further application - specific patents will be filed covering novel recipes, devices and
where possible processes employed.
12
Technology
•Use of standard adsorbents - formed
into hollow fibres (as opposed to beads)
•Perfect recipes and manufacturing
techniques to “spin” adsorbent fibres
from molecular sieving materials
targeting the removal of contaminants
from gas streams including:
- CO2, moisture, H2S , Helium,
Methane and hydrocarbons.
•Can be constructed as composite and
multilayered to tackle multi-component
contaminants.
•Patented design and manufacturing
process
Zeolite adsorbent crystals
Adsorbent hollow fibres
Project to develop
regenerative fibres
•Initial studies have shown that it is
possible to add an electrically
conductive outer layer to the fibres.
•Adding heat along the fibre speeds
up the process of regeneration.
•Faster cycle times will enable bed
size to be reduced.
•Zero purge air requirement for
regeneration (current technologies
use 20 – 25%)
Technology - benefits
Benefit Comment
High Efficiency
High surface area/volume ratio (>3000 m
2
/m
3
)
compared to state of the art monoliths (800-1000
m
2
/m
3
). Low vacuum/thermal swing requirements for
regeneration.
High added value products
The manufacturing process depends on the patented
technology and process know-how. Sales will be
targeted at high added value applications where there
are technical advantages over existing technology.
Lightweight, compact and low
energy use
Products can be configured and operated in many
ways, horizontally, vertically, or coiled. They are
particularly suitable for limited space, weight and power
applications.
Robust
Use of multiple layers enables high reliability products
to be fabricated that can withstand handling and
vibration during operation and maintenance.
2/05/07 15
Advantages
Large surface area, providing excellent kinetics
Minimal pressure drop as compared with packed bed technology
- Energy saving, Ease of breathing
No attrition, channeling, by pass within bed (no special filling technique)
Modules can be placed in any orientation
Fast regeneration due to open, accessible pore structure
Can remove multiple contaminants
2/05/07 16
•The maximum pressure drop reached by the packed bed (with 1.09 mm pellets) is
6000 Pa/m corresponding to an interstitial velocity of 1.2 m/s. The same pressure
drop figure (6000 Pa/m) is not reached in a NANPOR™ test hollow fibre module
(test unit dimensions of 50 fibres, 2.0mm diameter and 1.0 mm thickness) until
the interstitial velocity is approximately 17 m/s.
•That represents an increase in throughput of 1400%. For a given interstitial
velocity, the pressure drop of monolithic form and hollow fibre modules were
found to be considerably lower than that of a packed bed of same length.
•Even with less adsorbent weight stored within the hollow fibre modules (and
monoliths) compared to a similar dimensioned packed bed, their surface area will
allow for an improvement in adsorption performance for a comparable sized unit,
hence, the dp of the hollow fibre module is less and it’s performance is better than
a comparable packed bed.
Pressure drop
2/05/07 17
Low pressure drop characteristics of
modules compared with packed beds
0
1000
2000
3000
4000
5000
6000
7000
8000
9000
0 0.5 1 1.5 2 2.5
NANPOR module
Packed bed
Interstitial velocity, (m/s)
ΔP/L, (Pa/m)
Technology - status
The ability to spin long lengths of fibre
The ability to spin fibres in multiple layers
The ability to spin fibres which are mechanically
robust
The ability to produce modules which are easily
regenerated
Long lengths of fibre
Multiple layers
2/05/07 19
2/05/07 20
Adsorbent hollow fibres
2/05/07 21
Adsorbent fibres vs. packed (granular) bed
construction
Disadvantage Granular Bed Fibres
Settlement Yes No
Attrition Yes No
Channelling Yes No
Bypass Yes No
Orientation Vertical ONLY Any
Absorbent mixing Yes No
Capacity Low High (3-5 times)
Pressure loss High <5% of granular bed
Number of traps needed Up to 3 1
Flow direction One way only Either way (Poki-Yoki)