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Article

Efficient Air Desulfurization Catalysts Derived from Pig Manure Liquefaction Char

1
Department of Chemistry and Biochemistry, The City College of New York, New York, NY 10031, USA
2
Department of Civil, Architectural and Environmental Engineering, North Carolina A&T State University, 1601 E. Market St., Greensboro, NC 27411, USA
*
Author to whom correspondence should be addressed.
On leave from Department of Chemical Engineering, Maulana Azad National Institute of Technology Bhopal, Bhopal 462 003, India.
Received: 24 October 2017 / Revised: 15 November 2017 / Accepted: 17 November 2017 / Published: 20 November 2017
(This article belongs to the Special Issue Smart Carbon Materials in Catalysis)

Abstract

:
Biochar from the liquefaction of pig manure was used as a precursor of H2S desulfurization adsorbents. In its inorganic matter, it contains marked quantities of calcium, magnesium and iron, which are known as hydrogen sulfide oxidation catalysts. The char was used either as-received or mixed with 10% nanographite. The latter was added to increase both the content of the carbon phase and conductivity. ZnCl2 in two different ratios of char to an activation agent (1:1 and 1:2) was used to create the porosity in the carbon phase. The content of the later was between 18–45%. The activated samples adsorbed 144 mg/g H2S. Sulfur was the predominant product of reactive adsorption. Its deposition in the pore system and blockage of the most active pores ceased the materials’ activity. The presence of the catalytic phase was necessary but not sufficient to guarantee good performance. The developed porosity, which can store oxidation products in the resulting composite, is essential for the good performance of the desulfurization process. The surface of the composite with nanographite showed the highest catalytic activity, similar to that of the commercial Midas® carbon catalyst. The results obtained indicate that a high quality reactive adsorbent/catalyst for H2S removal can be obtained from pig manure liquefaction wastes.

1. Introduction

Waste remediation and toxic gas containment are among the problems which have to be addressed by a contemporary society. Many hazardous gases such as hydrogen sulfide (H2S) continue to be emitted by industrial plants, further compounding already existing environmental problems [1,2]. H2S affects various organ systems [3,4]. Its effects on the body can rapidly lead to death when exposed to high concentrations (over 1000 mg/m3) [5]. The above concerns have prompted environmental agencies to issue drastic exposure limits, and stimulated research to decrease the exposure to this gas. Hydrogen sulfide is one of the most common compounds found in petrochemical processing plants, the feedstock of syngas, and wastewater treatment plants. The efficient removal of H2S has been a major issue in industrial processes. Among the various sulfur removal techniques, adsorption on carbon-based materials at an ambient temperature and pressure has been found to be economical and cost-effective for medium and small-scale sulfur removal units [6,7,8,9].
In recent years, the novel idea of using biomass waste as a source of adsorbents of toxic gases and various liquids has been developed and research in this area is ongoing [10,11,12,13]. The term biochar has been used to refer to these increasingly popular and cost-effective materials. Biochar is the carbon-rich product of the thermal decomposition of organic matter in an inert atmosphere. Even though biochar and activated carbon (AC) have many similarities, they differ primarily in their preparation method, precursor material, and the resulting physical and chemical properties of the final products. With biomass waste being the feedstock, biochar becomes more energy-efficient and less cost-intensive than commercial activated carbons. In some cases, it can be an alternative adsorbent [14,15,16].
Various chemical activation agents, such as K2CO3 [17], H2SO4 [18], H3PO4 [19], and ZnCl2 [20], have been used to alter the physical properties of industrial waste-based adsorbents in order to increase their performance and to make it comparable to that of commercial grade carbons. Of course, all these methods add costs and make the competition with activated carbon less favorable.
Various municipal [21,22,23] and industrial [24,25,26] as well as animal manure [27,28,29] wastes have been used to produce adsorbents. Simple carbonization does not lead to an extensive surface area owing to a limited content of an organic matter and a high content of inorganic compounds, mainly in the sludges [30,31]. The highest area among the adsorbents obtained from sewage sludge was reported be 137 m2/g [32]. It is well known that chemical activation by ZnCl2 or H2SO4 increases the surface area of the manure-based adsorbents to as high as 555 m2/g [32,33]. Still, owing to the low content of an organic matter, there are limits to the porosity development in the sludge-based adsorbents. Nevertheless, some inorganic matter might bring important catalytic properties [34].
Due to its high organic content, animal manure seems to be an attractive precursor to develop adsorbents. It was reported that such materials can have similar pore structure parameters to those of activated carbon [35,36] and also alkaline surface chemistry [37]. These features make them suitable for adsorptive separations. Lima et al. [38] studied adsorbents derived from turkey litter and reported a maximum surface area of 472 m2/g and an adsorption capacity of 1.86 mmol Cu2+/g carbon. This capacity was superior to those obtained on two commercial carbons studied: Minotaur® (0.93 mmol Cu2+/g carbon) and PUR RF® (0.28 mmol Cu2+/g carbon). It is important to mention that both commercial carbons’ surface areas were much higher than that of the turkey-litter-derived materials. (Minotaur®—844 m2/g; PUR RF®—511 m2/g). The development of adsorbents with manure as a precursor also presents added benefits such as an agricultural sustainability and land restoration [39]. Additionally, the pyrolysis process, since it degrades bacteria and pathogens, also provides the added benefit of reducing environmental health effects [40,41].
Xu et al. [10] have explored the use of manure as a precursor of adsorbents of hydrogen sulfide. Their results showed that manure-derived biochars were more efficient than were those sewage-sludge-based adsorbents. Tests were conducted in moist conditions and the reported capacities were 47.5 mg/g for pyrolized sewage sludge and 65.4 mg/g for pig-manure-based chars. The superior performance of the latter was due to the higher surface basicity. Strong alkalinity and a rich inorganic content in both chars played a crucial role in the H2S uptake as well as in the catalytic formation of elemental sulfur and SO42−. The latter was formed on the surface, whereas the former was formed in the pores of the material. This was attributed to more O2 present on the outer surface, which oxidized H2S to SO42−, as opposed to limited O2 in the pores, which resulted in an incomplete oxidation of H2S to elemental sulfur. On the pyrolized sewage sludge, SO42− likely combined with Ca, forming an insoluble anhydride, whereas on pig manure char it was in the form of soluble SO42−.
In this work, composites were synthesized from a manure-derived carbonaceous material similar to biochar but not as carbon-rich. The char is a waste from a pig manure liquefaction process leading to bioresins [42]. The physical properties were modified using a zinc chloride (ZnCl2) activation and the addition of nanographite (NG). While the former was intended to increase the porosity, the latter was added to increase the carbon phase content and conductivity. The performance of the synthesized materials as adsorbents of H2S at ambient conditions was investigated. To understand the adsorption performance and to link it to surface features, various characterization techniques such as nitrogen adsorption measurements, thermogravimetric analysis, elemental analysis, and X-ray diffraction were employed.

2. Results and Discussion

Hydrogen sulfide breakthrough curves are shown in Figure 1 and the calculated breakthrough capacities and surface pH values are collected in Table 1. The breakthrough curves for all samples are relatively steep, indicating fast adsorption kinetics. Pyrolysis alone has little effect on the performance of the manure-derived composites. On the other hand, chemical activation and/or the addition of the NG phase, significantly increase the breakthrough time. The SO2 release data is shown in Figure 2. Concentrations as high as 0.3 ppm were detected for BM, AB, ABA-1, ABA-NG and ABA-NG2 (the names of the samples are defined in Section 3.1 and Section 3.2). Lower maximum concentrations were detected for ABA-1 (0.2 ppm) and ABA-NG1 (0.1 ppm). This finding highlights the ability of the materials to catalyze the formation of SO2 and also potentially retain the gas on their surfaces. For all experiments, once the inlet gas was closed (after 100 ppm H2S) and the system was purged with moist air, all sensor readings returned to zero within one minute.
Among the samples derived from only manure char (AB, ABA-1 and ABA-2) the best performance was found for ABA-2, on which 144 mg of H2S per gram of adsorbent was retained. The addition of nanographite improved the performance slightly, which might suggest that features other than the carbon content (it increased about 10%) govern the uptake of H2S. Though AB-NG showed a 100% increase in the performance compared to that of AB, the results for ABA-NG1 and ABA-NG2 were very similar to those obtained for ABA-1 and ABA-2. What is interesting here is that unlike for the samples without NG, the adsorption capacity on ABA-NG2 was about 10% smaller than that on ABA-NG1.
The best performing samples also have a high affinity to adsorb water. As indicated elsewhere, water is important to create a film in the pore structure in which hydrogen sulfide can dissociate in alkaline environment [43]. HS then undergoes the oxidation process to sulfur or SO2/SO3.
In all cases, ZnCl2 activation significantly improved the performance of manure-based bio-char. However, the values reported are not superior to some of those previously reported in the literature for catalytic commercial-activated carbons on which even 60 wt % of sulfur can be adsorbed [43]. Nevertheless, it is important to mention that the values are much higher than those measured under similar conditions on virgin activated carbons [43] and comparable to those on Centaur® or caustic impregnated carbons [44]. This in turn, indicates the potential merits of tailoring the properties of bio-char for applications other than soil enrichment.
To explain the good performance of the newly developed manure biochar-derived adsorbents, their surface was characterized in detail from the point of view of both porosity and chemistry. From the measured nitrogen adsorption isotherms (Figure 3), the parameters of the pore structure (Table 2) and pore size distributions were calculated (Figure 4).
The pyrolysis of the initial waste char resulted in an 80% (72 mg/g) increase in the surface area; the addition of nanographite further increased the surface area by 45% to 105 mg/g. Activation with ZnCl2 resulted in surface areas between 250 and 330 m2/g. The surface areas for ABA-1 and ABA-2 increased to 319 m2/g and 331 m2/g, respectively. The similar surface area of ABA-1 and ABA-2 indicate that an increase in the amount of ZnCl2 does not significantly affect the porosity. In fact, only a slight increase in the volume of micropores was found for ABA-2 in comparison with that of ABA-1. This might be related to the limited amount of the carbon phase, which undergoes the activation process. Nevertheless, as seen from Table 1, the carbon content in ABA-2 is about 10% higher than that in ABA-1. It should be noted that even though the addition of NG increases the carbon content of ABA by 10%, it does not lead to the same increase in the porosity. In fact, the surface area of BA-NG1 decreased about 24% in comparison to that of ABA-NG2. Interestingly, the pore volumes remain almost the same with or without NG, suggesting that nonporous NG does not undergo any chemical activation. On the other hand, a higher amount of activation agent results in apparently similar porosity to that of ABA-2, suggesting a higher extent of activation than that in ABA-NG1.
Exposure to H2S significantly decreased the porosity of the samples. This suggests the deposition of the oxidation/reaction products on the surface [45]. The biggest effect is noticed for ABA-NG1 and ABA-2. For these two samples the surface area decreased by 66% and 70%, respectively. These two carbons also exhibit the highest, and almost identical, performances as H2S adsorbents. These results suggest that even though the addition of NG led to a decrease in the surface area by 22% relative to ABA-2, it provided surface feature(s) which apparently resulted in the same performance as that of ABA-2. The trend in the decrease in the surface area for the activated samples is consistent with the trend in the H2S breakthrough capacity.
The pore-size distributions (Figure 4) show that AB and AB-NG are predominantly mesoporous. The distribution for BM was not calculated owing to the nonporous nature of this sample. The activation with ZnCl2 introduced some degree of microporosity to the materials, and it appears that this development of micropores in large part is responsible for the superior performance of the activated samples in the H2S adsorption process. After exposure to H2S, the micropores almost disappeared. A similar effect was noticed for the catalytic carbon Midas® [46]. This suggests that micropores are either filled by the products of oxidation or their entrances are blocked by these products. The volume of these micropores might be a limiting factor in the H2S removal process on our materials. Though a relationship between the two measured quantities definitely exists, it does not appear that the volume of micropores is directly proportional to the adsorption capacity. The data obtained only indicate that micropores favor the H2S adsorption. The H2S molecule has a critical diameter of 3.2 Å; therefore, based on the pore-size distributions, a pore restriction is not expected to occur during the H2S adsorption process on our manure-derived carbonaceous adsorbents. ABA-2 and ABA-NG2 still retained some micropore volume after H2S exposure.
Surface chemistry is another important factor that is expected to affect the H2S reactive adsorption. The pH values listed in Table 1 indicate the predominantly neutral nature of the adsorbents’ surfaces. The best-performing samples have pH values close to 7. This is above the pH threshold of 4.5, which was indicated previously as limiting the surface activity for HS-formation, which is followed by its oxidation either to SO2 or elemental sulfur [43]. The former is promoted when small pores are present and sulfur radicals, spatially separated in them, undergo oxidation to SO2 [46]. As a result of the H2S reactive adsorption, the surface pH values drop. The largest decrease/acidification is found for ABA-NG1 (3.3 units). Interestingly, on ABA-2, which exhibited the same H2S removal capacity as that of ABA-NG1, the pH dropped only about 1.5 units. This suggests the differences in the reactive adsorption mechanisms.
The surface species, which are mainly responsible for the average surface pH of our adsorbents are those present in an inorganic matter. As shown in Table 1, the inorganic matter consists of 55–82 wt % the biochar-derived adsorbents. The best-performing samples have around 65% of inorganic matter. This suggests that the hypothetically separated carbon phase, assuming that the porosity originates only from this phase, would have a surface area of about 1000 and 750 m2/g for ABA-2 and ABA-NG1, respectively. This calculation once again indicates that the latter sample is more active despite its lower surface area.
The results of the ICP (Inductively Coupled Plasma) analysis of the inorganic matter are summarized in Table 3. Only AB and the two best-performing samples were tested. The results for all three samples are very similar and the addition of 10% NG or ZnCl2 activation did not significantly change the inorganic phase. In activated samples, slightly more Zn is present as a leftover after the activation process. The inorganic phase contains marked amounts of Ca, Mg and Fe compounds. While the oxides of the two former compounds were identified previously as catalytic phases promoting H2S dissociation prior to its oxidation to sulfur [34,46,47], iron contributes to the oxidation of sulfur via redox reactions [48]. The same composition of inorganic phases can certainly contribute to the same capacities of ABA-2 and ABA-NG1, but certainly it is not a sufficient condition, since the capacity of AB is much lower. Since AB has a much greater inorganic phase than the other two, the quantity of an inorganic matter does not seem to be the factor determining the adsorption behavior. These results suggest that the porosity of the carbon phase has a dominant role. Even though the surface area of ABA-2 is higher than that of ABA-NG1, their volumes of micropores are very similar and this quantity can be a limiting factor, assuming that the inorganic phase provides sufficient catalytic activity. The analysis of the pore size distributions after H2S adsorption show clear pore blocking, and as a result, the pores are inaccessible almost to the same extent in ABA-2 and ABA-NG1 as a result of reactive adsorption process. The adsorption seems to cease when micropores become occupied or blocked. It is important to mention that in all cases the change in the porosity indicates the deposition of some H2S oxidation products in the pore system. They could be either sulfuric acid, elemental sulfur or sulfur salts [49].
The products of H2S reactive adsorption present in the pore system were analyzed by thermal analysis/mass spectrometry performed in an inert atmosphere. The TG (thermogravimetric) and corresponding DTG (differential thermogravimetric) curves are collected in Figure 5. The peaks on the DTG curves represent the removal of the specific species from the surface. Since the samples were synthesized at 900 °C, all changes observed at temperatures below that should be linked to H2S exposure. For the exhausted AB and AB-NG, the new weight loss appears at 200, 400 and about 600 °C. Based on the history of the samples, the decomposition temperature and the results published in the literature [45,49], we assign those peaks to the removal of sulfuric acid, elemental sulfur and SO3 from the decomposition of iron sulfate, respectively [50]. The peak related to the removal of elemental sulfur from BA at 400 °C is very sharp, which indicates the deposition of a rather small amount of sulfur on the external surface of this low porosity sample. On both BA and BA-NG, the pH decrease was noticed in spite of the small adsorbed amounts, which supports the formation of sulfuric acid. Interestingly, upon the addition of NG, less elemental sulfur is formed and more sulfur is oxidized to sulfuric acid, which might be linked to the higher volume of small pores. They were found to promote the oxidation of H2S to SO2 and SO3 [51].
The weight-loss pattern for all activated samples, regardless of the presence of NG are very similar. The weight loss at about 120 °C is related to the removal of water and physically adsorbed H2S/SO2. A broad peak between 200 and 400 °C (centered between 280 and 380 °C, depending on the sample) mainly represents the removal of elemental sulfur, although the removal of sulfuric acid close to 200 °C can also contribute to it [45]. However, the amount of the latter is rather small. A shift of the peak maximum for ABA-1 to the higher temperature compared to that for ABA-2 might be related to the smaller pores present in the former sample. In such a system, the removal of sulfur from them requires more energy. The formation of elemental sulfur as a product of reactive adsorption is more desired than that of sulfuric acid. The latter results in the classification of waste as hazardous when the surface pH decreases to less than 2.
To analyze the products of reactive adsorption in more detail, the high-resolution TA/MS analysis with the heating rate 2 °C/min was carried out on ABA-2 and ABA-NG1, initial and exhausted, which showed the best performance in H2S removal. The collected m/z thermal profiles for 18, 32 and 64 m/z are collected in Figure 6. They represent water, sulfur and sulfur dioxide, respectively. The trends in the 18 and 64 m/z can be directly linked to the removal of H2SO4. Indeed, as suggested above, the most intense peaks on these thermal profiles appear with maximum at about 250 °C and represent H2SO4, and then at the higher temperatures mainly sulfur is removed, which consists of the majority of the oxidation products.
The quantitative analysis of the weight loss can be a confirmation of the H2S reactive adsorption mechanism. The weight losses represented by the main peak for ABA-1-E, ABA-2-E, ABA-NG1-E and ABA-NG2-E are 10%, 10%, 7% and 9%, respectively. Based on the H2S breakthrough capacity, assuming that all H2S is converted to sulfur, the weight gain would be expected to be about 13%, 14%, 14% and 12%, respectively. Even though some SO2/H2SO4 must be formed based on the broadness of the peak and observed pH changes, it is in rather a small quantity and mostly reacted with inorganic matter from sulfates. Another reason for the discrepancy in the balance of sulfur is the formation of sulfides, as a result of a direct reaction of H2S with an inorganic matter. CaS and MgS are expected to decompose at temperatures higher than 1000 °C [52]. The results obtained indicate that elemental sulfur is a predominant product of surface reactions on our materials.
The mechanisms of H2S reactive adsorption can be summarized by the following reaction pathways:
H 2 S H S + H +
2 H S + 0.5 O 2 2 S + H 2 O
S + O 2     S O 2     S O 3
S O 3 + H 2 O     H 2 S O 4
C a O + H 2 S     C a S + H 2 O
M g O + H 2 S     M g S + H 2 O
The basic environment promotes the dissociation of hydrogen sulfide in the film of water and then HS-ions are oxidized either to sulfur, sulfur polymers or sulfur oxides, depending on their location in the pore system. Small isolated pores promote the formation of SO3 and sulfuric acid [43]. Some H2S is also expected to react with alkali earth metal oxides/salts forming sulfides.
Based on the chemistry and porosity, the mechanism of air desulfurization follows that on catalytic carbon Midas® [46]. That catalyst has the surface area of 1100 m2/g and 30% of calcium/magnesium oxides. The surface area of our materials and thus their pore volume is about 3–4 times less than that of Midas®. The H2S removal activity per unit surface area is 0.41, 0.43, 0.55 and 0.36 mg/m2 for ABA-1, ABA-2, ABA-NG1 and ABNG-2, respectively. Interestingly, for ABA-NG1 the value is similar to that on Midas® (0.6 mg/m2). It is important to mention that so far Midas® has been identified as the most efficient catalyst for oxidation of H2S from air. It is able to convert it to elemental sulfur and retains 60% of its weight in the pore system [53].
As indicated in our objectives we have added NG not only to increase the content of the carbon phase but also to increase the conductivity and thus the efficiency of an electron transfer, which is important for redox reactions governing H2S oxidation on the surface [54]. Indeed, the sheet resistance of the activated samples were 25, 43, 14 and 19 Ω for ABA-1, ABA-2, ABA-NG1 and ABA-NG2, respectively, as measured for their thin films on the gold chips. Since indeed an increase in conductivity was found upon the addition of NG, this, in conjunction with the other favorable features discussed above, can be the reason for ABA-NG1 effectiveness being close to that of Midas® carbon.
XRD analyses were conducted on the initial and exhausted materials, however they did not provide more details to further explain the superior performance of the activated samples as H2S adsorbents. The crystal structure of the exhausted samples remained unchanged in comparison to the initial one. This in fact supports the finding that the oxidation product is amorphous sulfur deposited in the pore system and formed sulfates/sulfides are either in the amorphous form or deposited as very small particles not detectable by XRD.

3. Materials and Methods

3.1. Materials

Pig-manure-derived char (BM), was recovered as a waste after a 280 °C hydrothermal treatment process [55,56]. This initial sample (BM) was subjected to various treatments including pyrolysis and chemical activation. Reagent grade ZnCl2 (>98% Aldrich, St. Louis, MO, USA) was used for the chemical activation and nanographite (NG) (Nano 24—Asbury Graphite Mills, Inc., Asbury, NJ, USA) was used to increase the conductivity and the carbon phase content of the composites.

3.2. Synthesis of the Composites

Pyrolysis of the BM was carried out in a horizontal furnace. A 3 g sample was placed into a crucible and heated to 900 °C at 10 °C/min in a N2 atmosphere. The maximum temperature was held for one hour and then the sample was allowed to cool down to room temperature under a nitrogen flow. The synthesized material is referred to as AB.
For the zinc chloride (ZnCl2) chemical activation, 7 g of the M sample were dispersed in 15 mL of either 3.4 M ZnCl2 or 6.8 M ZnCl2. The carbon to ZnCl2 ratio was either 1:1 or 1:2. The solution was stirred at 80 °C for about 15 min and then the remaining slurry was dried overnight at 120 °C. The dry solid was pyrolized at 900 °C at the same conditions at which sample AB was obtained. After pyrolysis, the sample was washed in a Soxhlet apparatus to remove all residual impurities and until a stable pH was reached and a test for chloride ions was negative. The washed sample was then dried at 100 °C and referred to as ABA-1 and ABA-2 for 1:1 and 1:2 ratios, respectively.
Composites with nanographite were prepared by mixing the BM sample with nanographite, NG. The amount of the latter was 10% (w/w) of the raw material (BM). The samples were dispersed in water and the solution was stirred at 80 °C for about 15 min. Then the remaining slurry was dried overnight at 120 °C. The dry solid was then pyrolized at 900 °C. This sample was referred to as AB-NG. As a next step, it was activated with ZnCl2 following the same procedure as that for the ABA-1 and ABA-2 samples. The activated composites are referred to as ABA-NG1 and ABA-NG2, where the digits 1 and 2 represent the ratio of the dry precursor mixtures to ZnCl2, respectively. The samples exposed to H2S in the dynamic test are referred to with the suffix ‘E’.

3.3. Methods

3.3.1. H2S Breakthrough Capacity

Adsorbent samples of a size between 0.4 and 0.6 mm were packed into a glass column (length: 370 mm; internal diameter: 9 mm) with a bed volume of 3.0 cm3. The H2S adsorption tests were carried out in moist conditions. Before the H2S test, the samples were pre-humidified with moist air (70% relative humidity at 25 °C) for two hours. The humid air containing 0.1% (1000 ppm) H2S was passed through a column of the adsorbent at a total flow rate of 500 mL/min. The H2S concentration was monitored from the outlet gas of the column by using a RAE MultiRae Plus monitoring system (RAE Systems, Inc., San Jose, CA, USA) with an electrochemical sensor. The H2S breakthrough curves were measured within the range of 0–100 ppm (100 ppm is the sensor limit). The amount of H2S adsorbed was calculated by the integration of the area above the breakthrough curves taking into account the mass of the sample, flow rate, concentration of H2S and time. Additionally, the sulfur dioxide (SO2) concentration as a possible H2S reaction byproduct, which might be released from the surface of the adsorbents, was recorded.

3.3.2. Evaluation of Porosity

Nitrogen adsorption isotherms were measured at −196 °C, using a ASAP 2020 (Micromeritics, Norcross, GA, USA) surface area and porosity analyzer. Prior to each measurement, initial samples were outgassed at 120 °C to vacuum 10−4 Torr. The surface area (SBET) and porosity of the samples were calculated from the measured isotherms. The volumes of pore and the pore-size distributions were calculated using the density functional theory (NLDFT) method based on heterogeneous pore sizes [57].

3.3.3. X-ray Diffraction (XRD)

The XRD measurements were obtained using a Phillips X’Pert X-ray diffractometer (PANalytical, Almelo, The Netherlands). The adsorbent was ground into a fine powder and analyzed by CuKα radiation at 40 kV and 40 mA.

3.3.4. Measurements of Electrical Resistance

A film of a sample dispersed N-methyl-2-pyrrolidone (NMP) was coated on a 0.5 cm × 0.45 cm gold interdigitated electrode. The samples were dried at 120 °C for 24 h to evaporate the NMP solvent. The sheet resistance was measured with a four-probe method using Keithley 2400 Multimeter (Keithley Instruments, Cleveland, OH, USA).

3.3.5. Thermal Analysis

Thermogravimetric (TG) curves were obtained using a SDT Q600 Simultaneous TGA/DSC Thermal Analyzer (TA Instruments, Newcastle, DE, USA). About 25 mg (of the initial and exhausted samples) were exposed to a heating rate of 10 °C/min up to 900 °C under a constant helium (He) flow of 100 mL/min. The differential thermogravimetric (DTG) curves were derived from the thermogravimetric (TG) curves. The high-resolution tests were performed in helium with a heating rate of 2 °C/min. Simultaneously, the m/z thermal profiles were recorded on a gas analysis system Omnistar GSD 320 (Pfeiffer Vacuum, Annecy, France).

4. Conclusions

The results obtained suggest that newly-developed biochar from pig manure liquefaction can be used as a source of catalytic adsorbents for hydrogen sulfide removal from air. The catalytic sites and developed porosity are needed to ensure good adsorption performance. It was achieved here by the ZnCl2 activation. The H2S removal capacity for our newly-developed, biochar-based reactive adsorbents was high and comparable to that of high surface-area, catalytic-activated carbons. The most active was the surface of the composite with 10% of NG and 1:1 activation agent ratio. The presence of high amounts of calcium and magnesium in pig manure along with the pores in the carbons phase is responsible for the good performance of ABA-NG1. The nanographite phase, although in a small quantity and not significantly affecting the surface features, increased the content of the carbon phase and thus the conductivity, which plays a role in redox reactions. The relatively small volume of micropores is identified as a factor limiting the performance. This suggests that by the addition of a porous carbon phase to pig manure, an upgrade in the performance is likely to be achieved for air desulfurization. Owing to the catalytic properties, there is no direct relationship between the overall porosity and the amount of H2S adsorbed. Oxidation to elemental sulfur is a desirable feature from the point of view of the spent adsorbent disposal and regeneration. The results suggest that by thermal treatment up to 400 °C, the adsorbents can be partially regenerated. This is owing to elemental sulfur being the major product of H2S reactive adsorption

Acknowledgments

Sundaramurthy Suresh is grateful to SERB Indo-US Postdoctoral Fellowship. The authors thank Albert Tamashausky of Asbury Carbon for nanographite sample and for help with ICP analysis. Experimental help of Karifala Kante is appreciated. The partnership between CCNY and North Carolina A & T was enabled by the National Science Foundation (Awards Nos.: 1150695 & 1546921).

Author Contributions

Rajiv Wallace prepared the experimental set up, helped with the synthesis of the samples, and their characterization, and wrote the paper draft. Sundaramurthy Suresh synthesized the samples, measured the performance, characterized the samples, collected the data, Elham H. Fini developed bio-char using thermochemical processing of pig manure, Teresa J. Bandosz designed the experimental steps, analyzed the data and worked on the final version of the paper.

Conflicts of interest

The authors declare no conflict of interest.

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Figure 1. H2S breakthrough curves for manure-derived samples in moist conditions.
Figure 1. H2S breakthrough curves for manure-derived samples in moist conditions.
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Figure 2. The concentration of SO2 released from the manure-derived samples during H2S breakthrough experiments in moist conditions.
Figure 2. The concentration of SO2 released from the manure-derived samples during H2S breakthrough experiments in moist conditions.
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Figure 3. Nitrogen adsorption isotherms for the initial and exhausted samples.
Figure 3. Nitrogen adsorption isotherms for the initial and exhausted samples.
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Figure 4. Pore-size distributions for the initial and exhausted samples.
Figure 4. Pore-size distributions for the initial and exhausted samples.
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Figure 5. TG (top) and DTG (bottom) curves for initial and exhausted samples.
Figure 5. TG (top) and DTG (bottom) curves for initial and exhausted samples.
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Figure 6. m/z thermal profiles for the best performing samples.
Figure 6. m/z thermal profiles for the best performing samples.
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Table 1. H2S breakthrough capacities, surface pH and carbon content for initial and exhausted samples.
Table 1. H2S breakthrough capacities, surface pH and carbon content for initial and exhausted samples.
SampleAsh Content (%)pHH2S Breakthrough Capacity (mg/g)Water Uptake (mg H2O/g)
BM598.10111
BM-E-7.90--
AB8210.02618
AB-E-8.32--
ABA-1706.42132137
ABA-1-E-4.32--
ABA-2667.30144150
ABA-2-E-5.77--
AB-NG709.161344
AB-NG-E-8.47--
ABA-NG1626.9114498
ABA-NG1-E-3.63--
ABA-NG2557.0512792
ABA-NG2-E-5.58--
Table 2. Pore-structure parameters calculated by nitrogen adsorption isotherms.
Table 2. Pore-structure parameters calculated by nitrogen adsorption isotherms.
SampleSBET (m2/g)VT (cm3/g)Vmic (cm3/g)Vmes (cm3/g)Vmic/VT
BM400.1200.12-
BM-E120.0700.07-
AB720.1500.15-
AB-E640.1600.16-
ABA-13190.250.130.120.52
ABA-1-E1770.270.020.250.07
ABA-23310.330.100.230.30
ABA-2-E1000.150.020.130.13
AB-NG1050.2400.24-
AB-NG-E870.250.020.230.08
ABA-NG12580.250.100.150.40
ABA-NG1-E860.140.010.130.07
ABA-NG23500.270.170.100.63
ABA-NG2-E1370.220.030.190.14
Table 3. Chemical composition of ash in AB and in the best performing samples: ABA-2 and ABA-NG1 (in wt %).
Table 3. Chemical composition of ash in AB and in the best performing samples: ABA-2 and ABA-NG1 (in wt %).
SampleABABA-2ABA-NG1
Al2O32.672.962.88
CaO58.9057.9656.77
CuO0.811.0471.21
Fe2O35.345.876.86
K2O1.350.240.27
MgO16.9016.4715.36
MnO20.680.590.62
Na2O0.920.540.46
SiO211.7112.4813.54
ZnO0.331.521.66

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Wallace, R.; Suresh, S.; Fini, E.H.; Bandosz, T.J. Efficient Air Desulfurization Catalysts Derived from Pig Manure Liquefaction Char. C 2017, 3, 37. https://doi.org/10.3390/c3040037

AMA Style

Wallace R, Suresh S, Fini EH, Bandosz TJ. Efficient Air Desulfurization Catalysts Derived from Pig Manure Liquefaction Char. C. 2017; 3(4):37. https://doi.org/10.3390/c3040037

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Wallace, Rajiv, Sundaramurthy Suresh, Elham H. Fini, and Teresa J. Bandosz. 2017. "Efficient Air Desulfurization Catalysts Derived from Pig Manure Liquefaction Char" C 3, no. 4: 37. https://doi.org/10.3390/c3040037

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