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High-Pressure Volumetric Analyzer · Ads/g (cc STP) Pressure (Bar) H 2 0 100 200 300 400 500 600...

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High-Pressure Volumetric Analyzer
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Page 1: High-Pressure Volumetric Analyzer · Ads/g (cc STP) Pressure (Bar) H 2 0 100 200 300 400 500 600 700 0 20 40 60 80 100 120 140 160 180 200 V ol Ads/g (cc STP) Pressure (Bar) AC1 Ads

The HPVA II software uses a National Instruments data acquisition interface to communicate with the analyzer. The data acquired during analyses are written to files that are read by a macro written in Microsoft Excel.

The macro uses the temperature and pressure data to obtain the correspond-ing compressibility factors from NIST REFPROP software to correct for the non-ideality of the high-pressure gases. Data reduction using the Excel macro provides reports as interactive spread-sheets which list the temperature and pressure data used for volume adsorbed calculations as well as excess isotherm, weight percentage, Langmuir theory, kinetic data plots, BET surface area, and total pore volume.

High-Pressure Volumetric Analyzer

Page 2: High-Pressure Volumetric Analyzer · Ads/g (cc STP) Pressure (Bar) H 2 0 100 200 300 400 500 600 700 0 20 40 60 80 100 120 140 160 180 200 V ol Ads/g (cc STP) Pressure (Bar) AC1 Ads

Dual free-space measurement for accurate isotherm data

Free space can be measured or entered

Correction for non-ideality of analysis gas using NIST REFPROP compressibility factors calculated from multiple equations of state

Reports provided as interactive spreadsheets

Isotherm and weight percentage plots created automatically

Tables of raw data used for report calculations

Real-time charts for Pressure vs. Time and Temperature vs. Time

Gas mixtures with up to three components can be used

Kinetic data provided for rate of adsorpotion calculations

Langmuir equation used to model Type I isotherms

High-precision, solid-state design high-pressure transducer provides a reading accuracy of ±0.04% full scale with a stablility of ±0.1%

Low-pressure pressure transducer provides a reading accuracy of ±0.15% of value

System can attain a maximum pressure of 200 bar

Hydrogen gas sensor automatically shuts down the system should a hydrogen leak occur

BET surface area, Langmuir surface area, and total pore volume calculations included

HPVA II Benefits・

High-Pressure Speciality Applications

High-Pressure Volumetric Analysis

The HPVA II Series of adsorption analyzers from Particulate Systemsuses the static volumetric method to obtain high-pressure adsorptionand desorption isotherms utilizing gases such as hydrogen, methane, and carbon dioxide.

The volumetric technique consists of introducing [dosing] a knownamount of gas [adsorptive] into the chamber containing the sampleto be analyzed. When the sample reaches equilibrium with the adsorbate gas, the final equilibrium pressure is recorded. These dataare then used to calculate the quantity of gas adsorbed by the sample.

This process is repeated at given pressure intervals until the maximum preselected pressure is reached. Then the pressure can be decreased to provide a desorption isotherm. Each of the resulting equilibrium points [volume adsorbed and equilibrium pressure] is plotted to provide an isotherm.

Excellent reproducibility and accuracy are obtained by using separate transducers for monitoring low and high pressures.

Page 3: High-Pressure Volumetric Analyzer · Ads/g (cc STP) Pressure (Bar) H 2 0 100 200 300 400 500 600 700 0 20 40 60 80 100 120 140 160 180 200 V ol Ads/g (cc STP) Pressure (Bar) AC1 Ads

Carbon Dioxide Sequestration

Typical HPVA II Applications

Hydrogen StorageDetermining the hydrogen storagecapacity of materials such as porouscarbons and metal organic frameworks(MOFs) is pivotal in the modern demandfor clean energy sources. These materialsare ideally suited for storage because they allow you to safely adsorb and desorb the hydrogen. Stored adsorbedhydrogen in MOFs has a higher energy density by volume than a gaseoushydrogen and does not require the cryogenic temperatures needed to maintain hydrogen in a liquid state. The HPVA II software provides a weight percentage plot that illustrates the amount of gas adsorbed at a given pressure as a function of the sample mass − the standard method for review-ing a sample’s hydrogen storage capacity.

Porous coal samples from underground beds can be analyzed with the HPVA II to determine their methane capacity at high pressures. This allows the user to find the methane adsorption and desorption properities of the underground coal beds, which is useful in determining approximate amounts of hydrocarbons available in coal-bed reserves. Kinetic data from the experiments can also show the rate of metane adsorption and desorption on these porous carbon samples at specific pressures and temperatures.

Coal-Bed Methane

High-pressure methane can be dosed onto shale samples to generate adsorption and desorption isotherms. This provides the methane capacity of the shale at specific pressures and temperatures. The adsorption isotherm can be used to calculate the Langmuir surface area and volume of the shale. The Langmuir surface area is the surface area of the shale assuming that the adsorbate gas forms a single layer of molecules. The Langmuir volume is the uptake of methane at infinite pressure − the maximum possible volume of methane that can be adsorbed to the surface of the sample.

Shale Gas

Wide Operating Pressure range: High Vacuum to 100 or 200 bar

Broad Temperature Capability: From cryogenic to 500 °C

Excellent control of sample temperature by means of a recirculating temperature bath, cryogen dewar, or furnace

Manifold temperature controlled with heater for stability and accuracy

Fully automated analysis using interactive software

Excellent data reproducibility

Handles typical adsorbates such as nitrogen, hydrogen, methane, argon, oxygen, and carbon dioxide

Comprehensive Data Analysis package using Microsoft® Excel® macros for data processing and graphing

Software includes NIST REFPROP

HPVA II Features

Evaluating the quantity of carbon dioxide that can be adsorbed by carbons and other materials is important in the ongoing study of carbon dioxide sequestration. High pressures obtained with the HPVA II can simulate the underground conditions of sites where CO2 is to be injected. Configuring the HPVA II with a chiller/heater bath allows the user to evaluate the CO2 uptake at a range of stable temperatures, providing data that can be used to calculate heats of adsorption. These isotherms are typically analyzed up to approximately 50 bar at near ambient temperatures due to CO2 condensation at higher pressures.

Page 4: High-Pressure Volumetric Analyzer · Ads/g (cc STP) Pressure (Bar) H 2 0 100 200 300 400 500 600 700 0 20 40 60 80 100 120 140 160 180 200 V ol Ads/g (cc STP) Pressure (Bar) AC1 Ads

Pressure TransducersTwo transducers are used to precisely measure the system pressure. A 1000- torr transducer is used to accurately monitor pressures below 1 atmosphere and is protected from high pressure with an isolation valve and a cracking valve that relieves to the vent.

Servo ValvesThe servo valves are used to automatically regulate flow of the gas in the manifold to the vent and vacuum.

Vacuum SystemConsists of a mechanical pump and internal Pirani vacuum gauge. User can provide their own pump or purchase the high-vacuum turbo pump package.

HPVA II System

Refrigerated/heated recirculation vessel [customer provides temperature control bath]

Four-liter, stainless-steel dewar for liquid cryogen

Furnance allows for experiments ranging up to 500 °C

Cryostat can precisely control sample temperatures from ambient conditions to 30 K

Four Methods of Sample Temperature Control

ManifoldAll the valves in the manifold are pneumatically operated, high-pressure valves with Kel-F® seats. Valve tubing is constructed with heavy wall, 316L stainless steel and is attached via a VCR connection or welded. The temperature of the insulated manifold region is stabilized using a heater controlled by an adjustable PID controller.

SYSTEM SCHEMATIC

Pres

sure

(bar

)

HIGH PRESSURE TRANSDUCER

LOW PRESSURETRANSDUCER

DEGASFURNACE

VACUUM GAUGE

Page 5: High-Pressure Volumetric Analyzer · Ads/g (cc STP) Pressure (Bar) H 2 0 100 200 300 400 500 600 700 0 20 40 60 80 100 120 140 160 180 200 V ol Ads/g (cc STP) Pressure (Bar) AC1 Ads

The HPVA II software uses a National Instruments data acquisition interface to communicate with the analyzer. The data acquired during analyses are written to files that are read by a macro written in Microsoft Excel.

The macro uses the temperature and pressure data to obtain the correspond-ing compressibility factors from NIST REFPROP software to correct for the non-ideality of the high-pressure gases. Data reduction using the Excel macro provides reports as interactive spread-sheets which list the temperature and pressure data used for volume adsorbed calculations as well as excess isotherm, weight percentage, Langmuir theory, kinetic data plots, BET surface area, and total pore volume.

0.00

0.02

0.04

0.06

0.08

0.10

0.12

0.14

0.16

0.00 0.05 0.10 0.15 0.20 0.25 0.30

1/[Q

(Po/

P - 1

)]

Relative Pressure (P/Po)

Data Reduction

Weight Percentage Uptake of H2 on MOF (CuBTC)

Nitrogen on Silica Alumina

BET Surface Area Plot, SiAl

0.00

5.00

10.00

15.00

20.00

25.00

30.00

200.0 220.0 240.0 260.0 280.0 300.0 320.0 340.0

Pres

sure

(bar

)

Time (min)

The decrease in pressure indicates the adsorption of the gas.

H2 Uptake on Cu(BTC) at 100K, Kinetic Data

H2 Uptake on Cu(BTC) at 100 K, Kinetic Data

H2 Uptake on Cu(BTC) at 100 K, Kinetic Data

0

50

100

150

200

250

300

350

400

450

0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1.0

Vol A

ds/g

(cc

STP)

Vo

l Ads

/g (c

c ST

P)

Pressure (Bar)

Time (min)

0

0.2

0.4

0.6

0.8

1

1.2

1.4

0 20 40 60 80 100 120 140 160 180 200

Pressure (Bar)

Pressure (Bar)

15.150

15.200

15.250

15.300

15.350

15.400

317.80 318.00 318.20 318.40 318.60 318.80 319.00 Time (min)

Pres

sure

(bar

)

Vol A

ds

as W

eig

ht

Per

cen

tag

e

Supplemental HPVA II Reporting

Page 6: High-Pressure Volumetric Analyzer · Ads/g (cc STP) Pressure (Bar) H 2 0 100 200 300 400 500 600 700 0 20 40 60 80 100 120 140 160 180 200 V ol Ads/g (cc STP) Pressure (Bar) AC1 Ads

30C 40C 50C

Pressure (Bar)

25C Des 50C Ads

50C Des

0

10

20

30

40

50

60

70

80

0 5 10 15 20 25 30 35 40 45

Vol A

ds/g

(cc

STP)

0

20

40

60

80

100

120

140

160

180

0 5 10 15 20 25 30 35 40 45

Vol A

ds/g

(cc

STP

)

Pressure (Bar)

30C Ads 50C Ads 70C Ads

0

5

10

15

20

25

0 10 20 30 40 50 60

Vol A

ds/g

(cc

STP)

Vol A

ds/g

(cc

STP)

Pressure (Bar)

CBM1 CBM2 CBM3 CBM4 CBM5 CBM6

0

1

2

3

4

5

6

0 20 40 60 80 100

Pressure (Bar)

Shale1 Shale2 Shale3 Shale 4

Pressure (Bar)Pressure (Bar)

Vol A

ds/g

(cc

STP)

CO2

HPVA II Reporting

Two Molecular Sieves at 25 °C Microporous Carbon at Various Temperatures

S-III Microporous Carbon at Various Temperatures

Four Di�erent Shales at 25 °CSix Di�erent Coal Bed Samples at 30 °C

0

20

40

60

80

100

120

140

0 5 10 15 20 25 30 35 40 45

Vol A

ds/g

(cc

STP

)

0C 25C 50C

Pressure (Bar)

Pressure (Bar)

Zeolite 5A at Various Temperatures

CH4

0

20

40

60

80

100

120

140

0 20 40 60 80 100 120

30C 40C 50C 60C

Pressure (Bar)

Vol A

ds/g

(cc

STP)

Page 7: High-Pressure Volumetric Analyzer · Ads/g (cc STP) Pressure (Bar) H 2 0 100 200 300 400 500 600 700 0 20 40 60 80 100 120 140 160 180 200 V ol Ads/g (cc STP) Pressure (Bar) AC1 Ads

Cryostat

0

20

40

60

80

100

120

140

0 20 40 60 80 100 120 140 160 180 200

Vol A

ds/g

(cc

STP)

Pressure (Bar)

0

100

200

300

400

500

600

700

800

900

0 1 2 3 4 5 6 7 8 9 10

Vol A

ds/g

(cc

STP)

Pressure (Bar) H2 Uptake at 30K

Zeolite 5A MOF (CuBTC) Microporous Carbon

Additional HPVA II Reporting

For extensive hydrogen storage studies at high pressures and low temperatures, the HPVA II can be interfaced with a cryostat to control analysis temperatures down to 30 K with a stability of ±0.003 K. The cryostat does not require liquid cryogens for operation; instead, it utilizes the Gifford-McMahon refrigeration cycle where pressurized helium is supplied from a compressor to produce cold temperatures. The HPVA II software communi-cates directly with the cryostat temperature controller allowing for precise temperature measurements recorded over the duration of the adsorption experiment. Generating hydrogen adsorption isotherms at multiple cryogenic temperatures presents researchers the advantage of more accurately calculating the isosteric heats of adsorption of hydrogen on their materials of study.

0

100

200

300

400

500

600

700

0 20 40 60 80 100 120 140 160 180 200

Vol A

ds/g

(cc

STP)

Pressure (Bar)

H2

0

100

200

300

400

500

600

700

0 20 40 60 80 100 120 140 160 180 200

Vol A

ds/g

(cc

STP)

Pressure (Bar)

AC1 Ads AC2 Ads

Various Materials at 30 K Two Activated Carbons at 77 K

MOF (CuBTC) at O °C

Page 8: High-Pressure Volumetric Analyzer · Ads/g (cc STP) Pressure (Bar) H 2 0 100 200 300 400 500 600 700 0 20 40 60 80 100 120 140 160 180 200 V ol Ads/g (cc STP) Pressure (Bar) AC1 Ads

Specifications

PO2/42700/00©All Rights Reserved 2013. Particulate Systems. Norcross GA 30093. Printed in U.S.A.

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