Multifunctional Purification and Sensing of Toxic Hydride Gases by

Mar 26, 2015 - ... Zhili Dong , Timothy J. White , Asel Sartbaeva , Ulrich Hintermair , and Valeska P. Ting ... Chinese Chemical Letters 2018 29 (6), ...
2 downloads 0 Views 869KB Size
Subscriber access provided by SETON HALL UNIV

Article

Multifunctional Purification and Sensing of Toxic Hydride Gases by CuBTC Metal-Organic Framework Gregory William Peterson, David K. Britt, Daniel T. Sun, John J. Mahle, Matthew A Browe, Tyler J Demasky, Shirmonda Smith, Amanda L Jenkins, and Joseph Anthony Rossin Ind. Eng. Chem. Res., Just Accepted Manuscript • DOI: 10.1021/acs.iecr.5b00458 • Publication Date (Web): 26 Mar 2015 Downloaded from http://pubs.acs.org on March 29, 2015

Just Accepted “Just Accepted” manuscripts have been peer-reviewed and accepted for publication. They are posted online prior to technical editing, formatting for publication and author proofing. The American Chemical Society provides “Just Accepted” as a free service to the research community to expedite the dissemination of scientific material as soon as possible after acceptance. “Just Accepted” manuscripts appear in full in PDF format accompanied by an HTML abstract. “Just Accepted” manuscripts have been fully peer reviewed, but should not be considered the official version of record. They are accessible to all readers and citable by the Digital Object Identifier (DOI®). “Just Accepted” is an optional service offered to authors. Therefore, the “Just Accepted” Web site may not include all articles that will be published in the journal. After a manuscript is technically edited and formatted, it will be removed from the “Just Accepted” Web site and published as an ASAP article. Note that technical editing may introduce minor changes to the manuscript text and/or graphics which could affect content, and all legal disclaimers and ethical guidelines that apply to the journal pertain. ACS cannot be held responsible for errors or consequences arising from the use of information contained in these “Just Accepted” manuscripts.

Industrial & Engineering Chemistry Research is published by the American Chemical Society. 1155 Sixteenth Street N.W., Washington, DC 20036 Published by American Chemical Society. Copyright © American Chemical Society. However, no copyright claim is made to original U.S. Government works, or works produced by employees of any Commonwealth realm Crown government in the course of their duties.

Page 1 of 22

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Industrial & Engineering Chemistry Research

Multifunctional Purification and Sensing of Toxic Hydride Gases by CuBTC Metal-Organic Framework Gregory W. Peterson,*† David Britt, ‡ Daniel T. Sun,‡ John J. Mahle, † Matthew Browe, † Tyler Demasky, θ Shirmonda Smith,θ Amanda Jenkins, θ and Joseph A. Rossin± †



Edgewood Chemical Biological Center, 5183 Blackhawk Rd., APG, Maryland 21010-5424,

The Molecular Foundry, Lawrence Berkeley National Laboratory, 1 Cyclotron Rd., Berkeley,

CA 94720; θLeidos, Inc. P.O. Box 68, Gunpowder, MD 21010-0068; ±Guild Associates, Inc., 5750 Shier-Rings Road, Dublin, OH 43016

*Corresponding author: Gregory W. Peterson, Email: [email protected]; Ph: (410) 436-9794

Abstract In this report we evaluate the metal-organic framework CuBTC as a real-world adsorbent for protection against three toxic hydride gases: ammonia, arsine, and hydrogen sulfide. We develop a scalable room-temperature synthesis of high surface area CuBTC using a benign ethanol-water solvent system. We test the capacity of CuBTC for the hydride gases under micro-breakthrough and real-world packed-bed conditions both dry and at high humidity. Under micro-breakthrough conditions CuBTC outperforms a broad spectrum carbon (BSC) adsorbent for uptake of ammonia and arsine, with approximately equivalent uptake of hydrogen sulfide. Under packedbed conditions CuBTC outperforms the BSC for ammonia uptake, but offers little protection 1 ACS Paragon Plus Environment

Industrial & Engineering Chemistry Research

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

against arsine or hydrogen sulfide. We demonstrate the potential for CuBTC to act not only as an effective adsorbent for ammonia, but also for sensing and to indicate saturation based on colorimetric and fluorescence changes. We find that CuBTC is a suitable material for inclusion in respiratory protective devices for protection against ammonia, with potential benefits against other hydride gases.

Keywords Ammonia, Arsine, Hydrogen Sulfide, CuBTC, HKUST-1, Metal-organic framework, Filtration

2 ACS Paragon Plus Environment

Page 2 of 22

Page 3 of 22

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Industrial & Engineering Chemistry Research

1. Introduction Toxic industrial chemicals are a significant hazard in both industrial and defense scenarios, as many pose inhalation hazards to first responders, industrial workers, and military personnel. Ammonia, arsine, and hydrogen sulfide gases, especially the latter two, are particularly toxic hydrides. All three gases are used industrially, and in many cases require respirators during use. In addition to required protection against these gases, technologies that can detect the chemicals or provide end-of-service-life indication of exhausted filters are beneficial to the end user. Due to their high volatility, all three gases require reactive moieties within sorbents for permanent chemical removal. Arsine and hydrogen sulfide can be oxidized by impregnants such as copper oxide and silver on activated carbon used in respirators.1 Ammonia, on the other hand, is removed by acid-base chemistry – typically a metal chloride,2, 3 sulfate4 or other material acidic sites. Heteroatoms can be added to carbon substrates for the removal of both arsine and ammonia.5, 6 In practice, however, these techniques pose potential issues with storage/aging, especially in the presence of humidity, where the impregnants degrade.7 Over the past several years, new materials have been investigated for ammonia, arsine, and hydrogen sulfide filtration. Metal-organic frameworks (MOFs) are a particularly interesting group of materials, as one can incorporate different metals within the secondary building units (SBU) as well as the functional group on the organic linkers.8-11 MOFs, and especially CuBTC, have been investigated for ammonia removal on multiple occasions.12,13, 14,15 Very limited work, however, has investigated larger scale testing of engineered particles representative of actual filters under conditions reflecting real world performance.16

3 ACS Paragon Plus Environment

Industrial & Engineering Chemistry Research

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Furthermore, almost no experimental work has focused on MOF development for filtration and/or detection of arsine and hydrogen sulfide. Thallapally and coworkers have investigated isotherms of hydrogen sulfide on FMOF-217 and Prussian blue analogs,18 and Bandosz and coworkers conducted some research on CuBTC/graphite oxide composites, finding that hydrogen sulfide formed copper sulfide at the active sites.19, 20 Huang et al. also investigated Znbased MOF composites.21 Additional work shows promising hydrogen sulfide uptake by CPO27-Ni22 and MIL-series of MOFs23, 24; however, the latter work focused on high pressures not typically seen in respirable environments. The literature is completely devoid of arsine studies on metal organic frameworks. CuBTC, or HKUST-1, is a well known MOF consisting of a copper paddlewheel secondary building unit with coordinatively unsaturated copper sites connected by organic trimesic acid linkers.25 Several experimental studies have suggested the ability of CuBTC to oxidize, or interact with, oxidizable chemicals such as carbon monoxide26 and nitric oxide.27 Theoretical calculations have been conducted on CuBTC for ammonia, phosphine, and hydrogen sulfide, but fail to account for reactivity.28 Thus, considering that chemicals such as hydrogen sulfide and arsine are oxidizable, CuBTC should provide an opportune medium for such reactions to occur. The objectives of this effort are to evaluate the readiness of CuBTC to be used in filtration applications and to understand potential trade-offs with other materials. To meet this objective, we develop scalable reaction conditions for the synthesis of CuBTC at room temperature in a benign solvent system. We measure the ability of CuBTC to remove ammonia, arsine, and hydrogen sulfide, both in microbreakthrough experiments and in packed beds simulating full scale respiratory filters. We elucidate the mechanism of each hydride gas removal, and further

4 ACS Paragon Plus Environment

Page 4 of 22

Page 5 of 22

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Industrial & Engineering Chemistry Research

probe the potential of the material for use as a sensor or end-of-service-life indicator for these toxic gases.

2. Experimental Section 2.1 Sample Preparation Large scale Cu3(BTC)2 synthesis was developed starting from a known literature procedure.29, 30 The reaction pH, solvent system, and rate of base addition were found to be important to obtain optimal surface area, reaction yield, and batch-to-batch reproducibility. In the optimized synthesis 149.4 g of Cu(NO3)2•2.5H2O and 129.2 g of trimesic acid were dissolved in separate 2 L mixtures of 7:3 ethanol:water. The solutions were mixed while stirring. A solution of 50 g NaOH in 2 L 7:3 ethanol:water was then added dropwise at room temperature while stirring. The clear blue solution changed to a light blue slurry during addition. The solution was stirred at room temperature for 1 hour after addition. The light blue products were isolated by centrifugation and purified by Soxhlet extraction using ethanol for 24 hours. The resulting light blue powder was dried in air and then heated in an oven at 80 °C. Granules of CuBTC were prepared for breakthrough testing using a Carver Press at 5000 psi, followed by crushing and sieving into 20×40 mesh granules. A broad spectrum carbon was provided by 3M in a 20×40 mesh granules for comparison purposes.

2.2 Nitrogen Uptake Nitrogen uptake was measured at 77K using a Micromeretics Tristar system. Samples were off-gassed at 150 °C overnight for approximately 16 hours. Surface area measurements were

5 ACS Paragon Plus Environment

Industrial & Engineering Chemistry Research

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

calculated using the Brunauer-Emmett-Teller (BET) method, and total pore volumes were calculated at a relative pressure of 0.975. 2.3 X-ray Photoelectron Spectroscopy XPS spectra were recorded using a Perkin Elmer Phi 570 ESCA/SAM system employing MgKα x-rays. All binding energies were referenced to the C1s photoelectron peak at 284.6 eV. Samples were placed on double-stick tape, placed in the chamber, and off-gassed for one hour, and then placed in the chamber for analysis. 2.4 Attenuated Total Reflectance – Fourier Transform Infrared Spectroscopy Attenuated total reflectance – Fourier transform infrared (ATR-FTIR) spectroscopy data were collected on composites using a Bruker Tensor 27 FTIR with a platinum accessory and a single reflection diamond crystal. The average of sixteen scans from 600-4000 cm-1 with background subtraction was collected. The instrument resolution was 4 cm-1. Samples were evaluated pre- and post- chemical exposure. 2.5 Chemical Micro-breakthrough Samples were evaluated for ammonia, arsine, and hydrogen sulfide capacity using a microbreakthrough system. The system has been described previously.8, 12 Briefly, a specific amount of chemical was injected into a ballast and subsequently pressurized to yield a concentration of 5000 mg/m3 for each of the chemicals. The ballast contents were then mixed with a diluent air stream containing the required moisture content, conditioned from a temperature-controlled saturator cell, at a rate necessary to achieve challenge concentrations between 1000 and 4000 mg/m3. The mixed stream then passed through a sorbent bed submerged in a temperature-

6 ACS Paragon Plus Environment

Page 6 of 22

Page 7 of 22

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Industrial & Engineering Chemistry Research

controlled water bath. Approximately 55 mm3 of each sample was packed into a 4 cm length and 4 mm diameter tube, and was tested as a powder under dry (0% relative humidity, RH) and humid (80% RH) conditions. Samples were pre-equilibrated at the test RH for approximately 12 hours. The effluent stream then passed through a continuously operating Hewlett-Packard 5890 Series II gas chromatograph equipped with a photoionization detector for ammonia and a flame photometric detector for sulfur dioxide. Other parameters for the testing are outlined in Table S1 (supplementary information). Loadings were calculated in mol/kg by integrating the breakthrough curves at saturation. The system exhibits approximately 10% deviation with respect to saturation loading.

2.6 Chemical Breakthrough Ammonia, arsine, and hydrogen sulfide breakthrough testing was conducted on packed beds of 20×40 mesh materials using a push-pull-vented breakthrough apparatus, a schematic of which is shown in Figure S1. Table S1 summarizes the testing parameters. Chemicals were evaluated at a constant volume concentration of 1000 ppm. For ammonia and hydrogen sulfide, neat gas was delivered from compressed cylinder via mass flow controllers and mixed with excess air at rates necessary to achieve the desired concentration. Arsine was delivered from a pre-mixed cylinder of 4%, which is below the lower explosive limit for the chemical, which is pyrophoric in air. The flow rate, temperature, and humidity of the diluent stream were controlled using a Miller Nelson HCS-401control unit. From the diluent stream, flow was pulled through packed beds by vacuum at a flow rate of 5.2 L/min, resulting in a residence time of approximately 0.15 seconds. Materials were evaluated as-received at 15% relative humidity (AR/15) and pre-equilibrated and 7 ACS Paragon Plus Environment

Industrial & Engineering Chemistry Research

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

tested at 80% relative humidity (80/80). Beds were packed via storm-filling into a 4.1 cm diameter tube with a total length of approximately 17 cm. For all chemicals, the challenge concentration was monitored using a Miran 1A infrared detector. The ammonia and arsine effluent was monitored semi-continuously using an Innova photoacoustic multi-gas monitor, and the hydrogen sulfide concentration was measured using a Hewlett Packard 6980 gas chromatograph equipped with a flame photometric detector.

2.7 Chemical Analysis by UV-vis Samples were analyzed in reflectance mode using a Perkin-Elmer Lambda Max UV-Vis-NIR Model 1050N8092301from 250-2500 nm at a scan rate of 659.4 nm/min. Slit widths were 2nm for the photomultiplier tube (PMT) and 12.5nm for the near infrared (NIR) wavelengths (cooled PbS detector). Samples were placed in a custom built powder holder made of black polyurethane with a Heraeus Suprasil 3100 window, this allowed the samples to be recovered after testing.

3

Results and Discussion

3.1 Breakthrough Testing Microbreakthrough curves and resulting loadings are illustrated in Figure 1. Ammonia (Figure 1a) curves show broad spectrum carbon (BSC) eluting almost immediately through the beds, reaching capacity in less than 2000 min/g. Ammonia does not begin eluting through CuBTC until after this weighted time. The resulting capacities for CuBTC are approximately 10 times and 5 times greater than that of BSC under dry and humid conditions, respectively. Both materials show better ammonia removal in humid conditions as compared to dry conditions. 8 ACS Paragon Plus Environment

Page 8 of 22

Page 9 of 22

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Industrial & Engineering Chemistry Research

This is typical, especially for activated carbons, as ammonia is absorbed by water within the pore structure. BSC arsine curves (Figure 1b) show steep ascent to the feed concentration under both dry and humid conditions, as does the CuBTC material under dry conditions. Of interest, however, is the humid CuBTC curve, which initially breaks through to greater than 60% of the feed, drops back down to approximately 20% of the feed, and then gradually re-ascends to the feed concentration over a long period of time. This behavior is likely attributed to mass transfer resistance or an initial activation requirement for the reaction to occur. In any case, the resulting capacity for CuBTC is significantly higher than BSC under both dry and humid conditions. The BSC material exhibits a huge capacity for hydrogen sulfide (Figure 1c) under dry conditions, eluting long after CuBTC at the same humidity. The resulting loading for BSC is 8.7 mol/kg, over double that of CuBTC, which exhibits a loading of 3.4 mol/kg. Under humid conditions, however, the CuBTC material outperforms the activated carbon, exhibiting a loading of 3.5 mol/kg as compared to the 3.0 mol/kg provided by the BSC.

9 ACS Paragon Plus Environment

Industrial & Engineering Chemistry Research

1

1

(b)

(a) 0.8

0.6

0.6

C/Co

C/Co

0.8

0.4

0.4

BSC Dry

BSC Dry BSC Wet CuBTC Dry CuBTC Wet

0.2

BSC Wet

0.2

CuBTC Dry CuBTC Wet

0

0 0

2000

4000 6000 8000 Weighted Time (min/g)

10000

1

20000

40000 60000 Weighted Time (min/g)

80000

100000

10

(c)

BSC Dry BSC Wet CuBTC Dry CuBTC Wet

8 Loading (mol/kg)

0.8

0

12000

0.6

C/Co

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Page 10 of 22

0.4

0.2

6

NH3 Dry NH3 Wet AsH3 Dry AsH3 Wet H2S Dry H2S Wet

(d)

4

2

0

0

0

5000

10000 15000 Weighted Time (min/g)

20000

BSC

CuBTC

Figure 1. Microbreakthrough curves for (a) ammonia, (b) arsine, and (c) hydrogen sulfide. Calculated loadings are shown in (d).

Clearly CuBTC exhibits capacities similar to the broad spectrum carbon; however, in filtration applications, low concentration protection also depends on mass transfer dynamics. Breakthrough curves of 10 mm packed beds of 20×40 mesh materials are shown in Figure 2. Under both low and high humidity conditions, CuBTC provides significantly better ammonia removal as compared to the BSC material. This is likely due to activity throughout the CuBTC structure, as previously discussed,12 whereas BSC simply contains impregnants on an inert

10 ACS Paragon Plus Environment

Page 11 of 22

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Industrial & Engineering Chemistry Research

carbon substrate, and is underutilized compared to the CuBTC. Furthermore, the humid ammonia curve through CuBTC is flatter than through BSC, indicating a higher capacity, but reduced mass transfer. This correlates well with microbreakthrough data, which showed exceedingly high ammonia capacity of the CuBTC material. The full bed performance of CuBTC under dry (AR/15) and humid (80/80) conditions is approximately 31,000 and 51,000 mg-min/m3, respectively, approximately 50% better than BSC, which shows capacities of 20,000 and 34,000 mg-min/m3, respectively. Arsine and hydrogen sulfide breakthrough curves tell a different story, however. Immediate breakthrough of arsine occurs for CuBTC under high humidity conditions, whereas the BSC material provides excellent removal capabilities. Yet, the material still exhibits significant capacity. Thus, it is apparent that the critical bed depth required to reduce the arsine concentration from 3200 mg/m3 to below toxic levels is just too large. Although the CuBTC curves do show some protection against hydrogen sulfide, the material provides significantly lower protection as compared to the broad spectrum carbon. Clearly there exists a discrepancy between the microbreakthrough and scaled breakthrough tests, as CuBTC is similar to BSC for capacity but not breakthrough time and Ct. One potential explanation lies in the size of the molecules; performance decreases for CuBTC as molecule size increases, as arsine is larger than hydrogen sulfide, which is larger than ammonia. Due to the high degree of microporosity of CuBTC and lack of mesoporosity,31 mass transfer may be inhibited in engineered packed beds, which typically require a feeder pore structure such as that found in BSC and other activated carbons.32 Another, related explanation deals with reaction mechanism, which is explored in the following section. Specifically, the byproducts formed during hydride gas removal may in fact block access to micropores, further reducing mass transfer to the active sites. 11 ACS Paragon Plus Environment

Industrial & Engineering Chemistry Research

200

100

(a)

BSC (AR/15)

BSC (80/80)

CuBTC (AR/15)

Effluent Conc. (mg/m )

Effluent Conc. (mg/m3)

150

(b)

BSC (AR/15)

BSC (80/80)

CuBTC (80/80)

100

50

0

CuBTC (AR/15) CuBTC (80/80) 50

0 0

50

100 Time (min)

200

150

0

50

100 Time (min)

150

200

400,000

50

(c)

(d)

350,000

40

NH3 (AR/15) NH3 (80/80) AsH3 (AR/15) AsH3 (80/80) H2S (AR/15) H2S (80/80)

Ct (mg-min/m3)

300,000 Effluent Conc. (mg/m3)

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Page 12 of 22

30

20 BSC (AR/15) BSC (80/80)

10

250,000 200,000 150,000 100,000

CuBTC (AR/15)

50,000

CuBTC (80/80)

0 0

50

100 Time (min)

150

0

200

BSC

CuBTC

Figure 2. Packed bed breakthrough testing for (a) ammonia, (b) arsine, and (c) hydrogen sulfide. The concentration-time (Ct) values to break are shown in (d).

3.2 Characterization and Mechanism An interesting property observed is the color change of CuBTC during exposure to the hydride gases. Figure 3 illustrates the color change associated with materials. CuBTC is well known to change color upon exposure to humidity, becoming a lighter blue/teal color. Exposure to ammonia results in a lighter blue color as compared to the baseline substrate, and arsine

12 ACS Paragon Plus Environment

Page 13 of 22

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Industrial & Engineering Chemistry Research

exposure results in a blue-green color, especially under dry conditions. Hydrogen sulfide exposure results in a dark brown material.

Figure 3. CuBTC color change upon exposure to hydride gases. UV-vis data showed significant changes upon binding and removal of the analyte. CuBTC and CuBTC post-gas exposure spectra are shown in Figure S2. The addition of ammonia results in a characteristic hypochromic shift of approximately 70 nm of the 500 nm band. Changes in the higher order structure of the bands in the NIR are also noted along with an ammonia peak around 2200 nm. When arsine is added to the CuBTC there is little change to the overall spectrum. Some additional higher order structure is seen with the addition of the arsine resulting from the interaction with the MOF. The addition of hydrogen sulfide results in dramatic hyperchromic shift to lower reflectance. This effect is so pronounced that all the reflectance is lost in the NIR with the addition of the hydrogen sulfide. This is most likely the result of the formation of copper sulfide (CuS), a black highly absorbing compound.16 In all, little spectral difference was seen between dry and humid samples for all chemicals. 13 ACS Paragon Plus Environment

Industrial & Engineering Chemistry Research

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Page 14 of 22

PXRD patterns are shown for CuBTC samples prior to and following exposure to the hydride gases in Figure S3. The CuBTC material exposed to ammonia under low RH conditions shows a decrease in the 7 2θ peak, while the same peak is completely gone for the humid sample, signifying reduced long-range order. Additional peaks are present at higher 2θ values for low humidity samples, and is more pronounced for the material at high humidity. The signal-to-noise ratio also decreases for both low and high humidity samples exposed to ammonia, with more degradation occurring for the humid sample. This behavior is confirmed by nitrogen isotherm data, shown in Figure 4. Compared to the baseline material, the ammonia material evaluated under dry conditions loses almost all of its surface area, while the humid sample has negligible nitrogen uptake. The surface area decreases from 1350 m2/g to 130 m2/g for the ammonia/dry sample, while the surface area of the ammonia/humid sample decreases to 4 m2/g, representing complete structure degradation. This behavior is consistent with previous efforts.12

FTIR

spectra, shown in Figure S4 indicate the presence of N-H stretching at 1560 cm-1 for ammoniadosed samples, and the presence of uncoordinated benzenetricarboxylate bonds at 1620 and 1260 cm-1 further indicate structural degradation occurring within the system.33 XPS data are consistent with ammonia,34 or potentially an ammonium ion; with the high vacuum of XPS, however, data suggest a strong binding to the surface. PXRD and nitrogen isotherm data for arsine-exposed samples are somewhat different than ammonia data. After low humidity testing, PXRD data show almost no structural degradation, with major long-range order peaks remaining intact after exposure, with the exception of a new peak around 13.5 2θ. Interestingly, however, several new peaks form at 22.7, 32.5, 55.2, 59.8 2θ without an increase in signal-to-noise, perhaps indicating the formation of a new species within the pore structure. Data for samples exposed to arsine under humid conditions show similar 14 ACS Paragon Plus Environment

Page 15 of 22

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Industrial & Engineering Chemistry Research

peaks forming, with additional structure collapse as evidenced by the loss of the 7 2θ peak and increased signal-to-noise. This can be explained by moisture destroying the structure, which is known to occur on the CuBTC. Nitrogen isotherm data confirm this for the humid sample, but also show a significant decrease in nitrogen uptake for the dry sample as well, resulting in surface areas of 12 and 66 m2/g, respectively. Although the decrease in surface area is explained by moisture exposure for the humid sample, the PXRD data for the dry samples shows that the structure remains intact. Thus, another phenomenon must be occurring. XPS data, shown in Figure 5, shows the formation of peaks consistent with the 3d photoelectron line for arsenic (III) oxide at 44.4 eV.35 Furthermore, there are no peak shifts in the copper 2p photoelectron lines, indicating no change in speciation at that site. Instead, it is likely that the copper is providing a site for oxidation of arsine, which transforms into As2O3. On an atomic basis, as summarized in Table 1, there are 0.56 As atoms per copper atom under low RH conditions, and 0.41 As atoms per copper atom under humid conditions. The formation of arsenic oxide likely partially blocks pore apertures or further access to the copper site, thus explaining the reduced mass transfer kinetics in the packed bed test. The formation of As2O3 is further supported by the FTIR spectra (Figure S3), which shows a broad peak forming under both dry and humid conditions at approximately 800 cm-1, consistent with an As(III)-O symmetric stretch.36 PXRD data for hydrogen sulfide show more in common with ammonia as compared to arsine. Under both low and high humidity conditions, structural breakdown occurs as evidenced by the loss of the 7 2θ peak. An additional phase is obvious for the humid sample, and both dry and humid samples show reduced signal-to-noise. In conjunction with the nitrogen isotherm data, it is apparent that the structure is collapsing upon exposure to hydrogen sulfide, with reductions in surface area to 48 and 11 m2/g for low and high humidity samples, respectively. 15 ACS Paragon Plus Environment

Industrial & Engineering Chemistry Research

Whereas arsine was completely oxidized within the pore structure, hydrogen sulfide seems to directly, and permanently, react with the undercoordinated copper site of the SBU. XPS data show a large shift in the copper 2p3/2 photoelectron line, corresponding to either Cu2S37 or CuS.38 Similarly, the sulfur 2p3/2 peak shows the potential for both peaks,37, 39 along with the formation of S8.40 In fact, it is possible that all three species are forming. Clearly the copper speciation is changing as shown by XPS data (Figure 5); however, the brown color formation allows for the possibility of yellow S8 forming as well. Furthermore, the significantly reduced efficacy of packed bed filtration of hydrogen sulfide as compared to the microbreakthrough capacity test suggests that either pore blockage or blockage of access to copper sites occurs after initial hydrogen sulfide formation. If it was simply due to reaction with the copper sites, we would expect similar behavior for ammonia, in which polymerization or oxidation does not occur. FTIR (Figure S3) lends little insight, other than formation of peaks at approximately 1710 cm-1, which are consistent with benzenetricarboxylate.19

400 350 N2 Uptake at STP (cc/g)

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

300

CuBTC CuBTC_NH3 Dry CuBTC_NH3 Wet CuBTC_AsH3 Dry CuBTC_AsH3 Wet CuBTC_H2S Dry CuBTC_H2S Wet

250 200 150 100 50 0 0

0.2

0.4

0.6

0.8

1

p/p0

Figure 4. Nitrogen isotherms of exposed CuBTC as compared to the baseline material.

16 ACS Paragon Plus Environment

Page 16 of 22

Page 17 of 22

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Industrial & Engineering Chemistry Research

(a)

(b)

CuBTC_AsH3 AR15 CuBTC_AsH3 8080

CuBTC_NH3 Dry CuBTC_NH3 Wet 408

403

398

52

393

50

48

46

44

42

40

38

eV

eV

(c)

(d)

CuBTC CuBTC_H2S Dry CuBTC_H2S Wet

CuBTC CuBTC_H2S Dry CuBTC_H2S Wet 940

938

936

934

932

930

169

167

165

eV

163 eV

161

159

157

155

Figure 5. X-ray photoelectron spectra. (a) N 1s photoelectron spectra, (b) As 3d photoelectron spectra, (c) Cu 2p3/2 photoelectron spectra, and (d) S 2p3/2 photoelectron spectra.

Table 1. Atomic ratios for exposed CuBTC samples. NH3 AsH3 H 2S Dry Wet Dry Wet Dry Wet Cu/C 0.22 0.1 0.1 0.1 0.1 0.1 0.2 O/C 0.67 0.4 0.6 0.6 0.6 0.5 0.6 O/Cu 3.03 3.6 9.4 5.1 4.5 4.2 2.9 Hetero*/Cu 0.4 1.4 0.6 0.4 0.8 1.0 *Refers to the heteroatom in the hydride – either nitrogen, arsenic, or sulfur. Ratio

CuBTC

17 ACS Paragon Plus Environment

Industrial & Engineering Chemistry Research

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

4

Conclusion The difference in capacity and packed bed performance measurements for CuBTC and a

broad spectrum carbon were found to be substantial for three hydride gases. When considering capacity, CuBTC generally outperforms the carbon, yet the opposite is true for packed bed breakthrough tests with the exception of ammonia. This is likely due to mass transfer limitation associated with the larger molecular size of hydrogen sulfide and arsine as compared to ammonia, as well as the mechanism of reaction. Ammonia directly interacts with various structural areas of the CuBTC material, including undercoordinated copper sites and structural bonds between the SBU and organic linker. Hydrogen sulfide reacts similarly to the undercoordinated copper sites, but does not undergo the acid-base reaction with SBU/organic linkers. Thus, the capacity is lower for hydrogen sulfide as compared to ammonia on CuBTC, and the reduced kinetics of mass transfer and reaction result in lower packed bed performance as compared to the activated carbon. Arsine seemingly does not react with any portion of the substrate, but rather oxidizes to form arsenic trioxide. Although the capacity is sufficiently high, the combination of arsine size and the formation of these oxides within the pore structure result in significantly reduced performance in a packed bed. In addition to the performance of CuBTC, spectral signatures indicate potential use as sensors, with infrared and UV/Vis changes occurring after exposure to all three chemicals. Although there are potential shortcomings in protection against arsine and hydrogen sulfide, CuBTC does indeed provide substantial protection against ammonia, and thus any additional chemical removal is beneficial. The ability of this material to filter ammonia, in conjunction with the ability to scale to larger quantities makes CuBTC ready for transition to end-item 18 ACS Paragon Plus Environment

Page 18 of 22

Page 19 of 22

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Industrial & Engineering Chemistry Research

filtration applications. Future research will investigate tuning of pore and granule structure to optimize mass transfer for molecules larger than ammonia, as reaction mechanisms are clearly present.

Acknowledgements This work was conducted under Defense Threat Reduction Agency (DTRA) Project BA07PRO104. Supporting Information Available: Microbreakthrough and breakthrough testing conditions, UV/VIS spectra for exposed samples, PXRD data for exposed samples, and FTIR data for exposed samples. This information is available free of charge via the Internet at http://pubs.acs.org.

References 1. Quinn, R.; Dahl, T. A.; Diamond, B. W.; Toseland, B. A., Removal of arsine from synthesis gas using a copper on carbon adsorbent. Ind. Eng. Chem. Res. 2006, 45, 6272-6278. 2. Petit, C.; Karwacki, C.; Peterson, G.; Bandosz, T. J., Interactions of ammonia with the surface of microporous carbon impregnated with transition metal chlorides. J. Phys. Chem. C 2007, 111, 1270512714. 3. Romero, J. V.; Smith, J. W. H.; Sullivan, B. M.; Mallay, M. G.; Croll, L. M.; Reynolds, J. A.; Andress, C.; Simon, M.; Dahn, J. R., Gas Adsorption Properties of the Ternary ZnO/CuO/CuCl2 Impregnated Activated Carbon System for Multigas Respirator Applications Assessed through Combinatorial Methods and Dynamic Adsorption Studies. ACS Comb. Sci. 2011, 13, 639-645. 4. Glover, T. G.; Peterson, G. W.; DeCoste, J. B.; Browe, M. A., Adsorption of Ammonia by Sulfuric Acid Treated Zirconium Hydroxide. Langmuir 2012, 28, 10478-10487. 5. Petit, C.; Peterson, G. W.; Mahle, J.; Bandosz, T. J., The effect of oxidation on the surface chemistry of sulfur-containing carbons and their arsine adsorption capacity. Carbon 2010, 48, 1779-1787. 6. Petit, C.; Kante, K.; Bandosz, T. J., The role of sulfur-containing groups in ammonia retention on activated carbons. Carbon 2010, 48, 654-667.

19 ACS Paragon Plus Environment

Industrial & Engineering Chemistry Research

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

7. Rossin, J. A.; Morrison, R. W., The effects of molybdenum on stabilizing the performance of an experimental copper/zinc impregnated, activated carbon. Carbon 1993, 31, 657-9. 8. Glover, T. G.; Peterson, G. W.; Schindler, B. J.; Britt, D.; Yaghi, O., MOF-74 building unit has a direct impact on toxic gas adsorption. Chem. Eng. Sci. 2011, 66, 163-170. 9. Tanabe, K. K.; Wang, Z.; Cohen, S. M., Systematic Functionalization of a Metal−Organic Framework via a Postsynthetic Modification Approach. J. Am. Chem. Soc. 2008, 130, 8508-8517. 10. Deng, H.; Doonan, C. J.; Furukawa, H.; Ferreira, R. B.; Towne, J.; Knobler, C. B.; Wang, B.; Yaghi, O. M., Multiple Functional Groups of Varying Ratios in Metal-Organic Frameworks. Science 2010, 327, 846850. 11. Bloch, E. D.; Britt, D.; Lee, C.; Doonan, C. J.; Uribe-Romo, F. J.; Furukawa, H.; Long, J. R.; Yaghi, O. M., Metal Insertion in a Microporous Metal−Organic Framework Lined with 2,2′-Bipyridine. J. Am. Chem. Soc. 2010, 132, 14382-14384. 12. Peterson, G. W.; Wagner, G. W.; Balboa, A.; Mahle, J.; Sewell, T.; Karwacki, C. J., Ammonia Vapor Removal by Cu(3)(BTC)(2) and Its Characterization by MAS NMR. J. Phys. Chem. C 2009, 113, 1390613917. 13. Huang, L.; Bandosz, T.; Joshi, K. L.; van Duin, A. C. T.; Gubbins, K. E., Reactive adsorption of ammonia and ammonia/water on CuBTC metal-organic framework: A ReaxFF molecular dynamics simulation. J. Chem. Phys. 2013, 138. 14. Borfecchia, E.; Maurelli, S.; Gianolio, D.; Groppo, E.; Chiesa, M.; Bonino, F.; Lamberti, C., Insights into Adsorption of NH3 on HKUST-1 Metal-Organic Framework: A Multitechnique Approach. J. Phys. Chem. C 2012, 116, 19839-19850. 15. Saha, D. P.; Deng, S. G., Ammonia adsorption and its effects on framework stability of MOF-5 and MOF-177. J. Colloid Interface Sci. 2010, 348, 615-620. 16. Peterson, G. W.; DeCoste, J. B.; Grant Glover, T.; Huang, Y.; Jasuja, H.; Walton, K. S., Effects of Pelletization Pressure on the Physical and Chemical Properties of the Metal-Organic Frameworks Cu3(BTC)2 and UiO-66. Microporous Mesoporous Mater., 2013, 179, 48-53. 17. Fernandez, C. A.; Thallapally, P. K.; Motkuri, R. K.; Nune, S. K.; Sumrak, J. C.; Tian, J.; Liu, J., GasInduced Expansion and Contraction of a Fluorinated Metal−Organic Framework. Cryst. Growth Des. 2010, 10, 1037-1039. 18. Thallapally, P. K.; Motkuri, R. K.; Fernandez, C. A.; McGrail, B. P.; Behrooz, G. S., Prussian Blue Analogues for CO2 and SO2 Capture and Separation Applications. Inorg. Chem. 2010, 49, 4909-4915. 19. Petit, C.; Mendoza, B.; Bandosz, T. J., Hydrogen Sulfide Adsorption on MOFs and MOF/Graphite Oxide Composites. Chemphyschem 2010, 11, 3678-3684. 20. Petit, C.; Levasseur, B.; Mendoza, B.; Bandosz, T. J., Reactive adsorption of acidic gases on MOF/graphite oxide composites. Microporous Mesoporous Mater.2012, 154, 107-112. 21. Huang, Z.-H.; Liu, G.; Kang, F., Glucose-Promoted Zn-Based Metal-Organic Framework/Graphene Oxide Composites for Hydrogen Sulfide Removal. Acs App. Mater. Interfaces 2012, 4, 4942-4947. 22. Chavan, S.; Bonino, F.; Valenzano, L.; Civalleri, B.; Lamberti, C.; Acerbi, N.; Cavka, J. H.; Leistner, M.; Bordiga, S., Fundamental Aspects of H2S Adsorption on CPO-27-Ni. J. Phys. Chem. C 2013, 117, 1561515622. 23. Hamon, L.; Vimont, A.; Serre, C.; Devic, T.; Ghoufi, A.; Maurin, G.; Loiseau, T.; Millange, F.; Daturi, M.; Ferey, G.; De Weireld, G., Study of hydrogen sulphide adsorption on MIL-47(V) and MIL-53(Al, Cr, Fe) Metal-organic frameworks by isotherm measurements and in-situe experiments. In Characterisation of Porous Solids Viii, Kaskel, S.; Llewellyn, P.; RodriguezReinoso, F.; Seaton, N. A., Eds. 2009; pp 25-31. 24. Hamon, L.; Leclerc, H.; Ghoufi, A.; Oliviero, L.; Travert, A.; Lavalley, J.-C.; Devic, T.; Serre, C.; Ferey, G.; De Weireld, G.; Vimont, A.; Maurin, G., Molecular Insight into the Adsorption of H2S in the Flexible MIL-53(Cr) and Rigid MIL-47(V) MOFs: Infrared Spectroscopy Combined to Molecular Simulations. J. Phys. Chem. C 2011, 115, 2047-2056. 20 ACS Paragon Plus Environment

Page 20 of 22

Page 21 of 22

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

Industrial & Engineering Chemistry Research

25. Chui, S. S. Y.; Lo, S. M. F.; Charmant, J. P. H.; Orpen, A. G.; Williams, I. D., A chemically functionalizable nanoporous material [Cu3(TMA)2(H2O)3]n. Science (Washington, D. C.) 1999, 283, 1148-1150. 26. Rubes, M.; Grajciar, L.; Bludsky, O.; Wiersum, A. D.; Llewellyn, P. L.; Nachtigall, P., Combined Theoretical and Experimental Investigation of CO Adsorption on Coordinatively Unsaturated Sites in CuBTC MOF. ChemPhysChem 2012, 13, 488-495. 27. Bordiga, S.; Regli, L.; Bonino, F.; Groppo, E.; Lamberti, C.; Xiao, B.; Wheatley, P. S.; Morris, R. E.; Zecchina, A., Adsorption properties of HKUST-1 toward hydrogen and other small molecules monitored by IR. Phys. Chem. Chem. Phys. 2007, 9, 2676-2685. 28. Supronowicz, B.; Mavrandonakis, A.; Heine, T., Interaction of Small Gases with the Unsaturated Metal Centers of the HKUST-1 Metal Organic Framework. J. Phys. Chem. C 2013, 117, 14570-14578. 29. Majano, G.; Pérez-Ramírez, J., Scalable Room-Temperature Conversion of Copper(II) Hydroxide into HKUST-1 (Cu3(btc)2). Adv. Mater. 2013, 25, 1052-1057. 30. Thi, T. V. N.; Luu, C. L.; Hoang, T. C.; Nguyen, T.; Bui, T. H.; Nguyen, P. H. D.; Thi, T. P. P., Synthesis of MOF-199 and application to CO 2 adsorption. Adv. Nat. Sci.: Nanosci. Nanotechnol. 2013, 4, 035016. 31. Peterson, G. W.; DeCoste, J. B.; Glover, T. G.; Huang, Y.; Jasuja, H.; Walton, K. S., Effects of pelletization pressure on the physical and chemical properties of the metal-organic frameworks Cu3(BTC)(2) and UiO-66. Microporous Mesoporous Mater.2013, 179, 48-53. 32. Teng, H. S.; Hsieh, C. T., Influence of surface characteristics on liquid-phase adsorption of phenol by activated carbons prepared from bituminous coal. Ind. Eng. Chem. Res. 1998, 37, 3618-3624. 33. Bashkova, S.; Bandosz, T. J., Effect of surface chemical and structural heterogeneity of copper-based MOF/graphite oxide composites on the adsorption of ammonia. J. Colloid Interface Sci. 2014, 417, 109114. 34. Hendrickson, D. N.; Hollander, J. M.; Jolly, W. L., Nitrogen ls electron binding energies. Correlations with molecular orbital calculated nitrogen charges. Inorg. Chem. 1969, 8, 2642-2647. 35. Bahl, M. K.; Woodall, R. O.; Watson, R. L.; Irgolic, K. J., Relaxation during photoemission and LMM auger decay in arsenic and some of its compounds. J. Chem. Phys. 1976, 64, 1210-1218. 36. Connon, S. A.; Koski, A. K.; Neal, A. L.; Wood, S. A.; Magnuson, T. S., Ecophysiology and geochemistry of microbial arsenic oxidation within a high arsenic, circumneutral hot spring system of the Alvord Desert. FEMS Microbiol. Ecol. 2008, 64, 117-128. 37. Strohmeier, B. R.; Leyden, D. E.; Field, R. S.; Hercules, D. M., Surface spectroscopic characterization of Cu/Al2O3 catalysts. J. Catal. 1985, 94, 514-530. 38. Deroubaix, G.; Marcus, P., X-ray photoelectron-spectroscopy analysis of copper and zinc-oxides and sulfides. Surf. Interface Anal. 1992, 18, 39-46. 39. Perry, D. L.; Taylor, J. A., X-ray photoelectron and auger spectrscopic studies of Cu2S and CuS. J. Mater. Sci. Lett. 1986, 5, 384-386. 40. Hollinger, G.; Kumurdjian, P.; Mackowski, J. M.; Pertosa, P.; Porte, L.; Duc, T. M., ESCA study of molecular GeS3-xTexAs2 glasses. J. Electron Spectrosc. Relat. Phenom. 1974, 5, 237-245.

TOC Image 21 ACS Paragon Plus Environment

Industrial & Engineering Chemistry Research

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60

22 ACS Paragon Plus Environment

Page 22 of 22