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ZHONGXI Testing has obtained inspection qualification certifications from multiple countries and regions worldwide. We possess a senior testing team and advanced testing methods, providing independent, impartial, and professional third-party verification services for global carbon projects.
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Activated semi‑coke (ASC) – a carbonaceous adsorbent produced by the partial gasification or activation of coal‑based semi‑coke – has become an important material for flue gas desulfurization (FGD), denitrification (DeNOx), mercury removal, and the purification of wastewater and industrial gases. Its performance is governed by a unique combination of specific surface area, pore architecture (micro‑ and mesoporosity), surface chemistry (oxygen‑containing functional groups, basic sites), mechanical strength, sulfur capacity, and resistance to attrition and moisture. Unlike conventional activated carbons, ASC offers a lower cost, higher mechanical strength, and a balanced pore structure that favours the removal of SO₂, H₂S, and other acid gases. However, batch‑to‑batch variations in the activation conditions, the coal source, and the processing parameters can lead to significant differences in adsorption capacity, selectivity, and service life. Therefore, a rigorous, multi‑parametric analytical evaluation is indispensable for material qualification, process optimisation, quality assurance, and troubleshooting of field performance issues. Our ISO/IEC 17025‑accredited laboratory offers a dedicated, high‑depth testing service specifically tailored for activated semi‑coke adsorbents, integrating advanced physical, chemical, thermal, and dynamic performance methods to deliver a complete functional and safety fingerprint – far beyond routine iodine number or simple hardness tests.

Clients seeking our testing services typically aim to: (i) quantify the specific surface area, micropore volume, and mesopore volume to predict the adsorption capacity and the diffusion kinetics of the target pollutants, (ii) evaluate the breakthrough sulfur capacity and the total sulfur uptake under realistic gas compositions (including SO₂, O₂, H₂O, and CO₂), (iii) assess the mechanical strength and attrition resistance to ensure reliable operation in moving‑bed or fluidised‑bed reactors, (iv) measure the ignition temperature and thermal stability to guarantee safe handling and regeneration, (v) determine the surface basicity and the presence of active functional groups that contribute to the chemisorption of acidic gases, (vi) analyse the elemental composition and the ash content (including trace metals that may act as catalysts or poisons), (vii) evaluate the moisture content and the particle size distribution to predict the pressure drop and the dust generation, and (viii) generate robust data for product certification, supplier qualification, and regulatory compliance. Standard single‑parameter tests such as single‑point BET or a simple sulfur capacity measurement are insufficient because the real‑world performance of ASC depends on the synergistic interplay of pore architecture, surface chemistry, mechanical durability, and thermal behaviour, all of which require a suite of complementary techniques. Our integrated platform combines N₂ and CO₂ physisorption (BET, DFT, BJH) for surface area and porosity, mercury intrusion porosimetry for macroporosity, dynamic breakthrough testing with online UV‑fluorescence or FTIR for SO₂/H₂S capacity, Thermogravimetric Analysis (TGA) coupled with differential scanning calorimetry (DSC) and mass spectrometry (MS) for thermal stability and ignition temperature, mechanical crush strength and attrition testing (ASTM D4058, D5757), X‑ray fluorescence (XRF) and inductively coupled plasma mass spectrometry (ICP‑MS) for elemental composition, X‑ray diffraction (XRD) for mineral phase identification, Fourier‑transform infrared spectroscopy (DRIFTS) for surface functional groups, and laser diffraction for particle sizing – providing a complete and actionable quality profile.
We measure the BET‑specific surface area and the total pore volume by N₂ physisorption at 77 K over a wide relative pressure range (10⁻⁶–0.995), with a reproducibility of ±1.5%. The pore size distribution is derived using NLDFT, QSDFT, and BJH models to characterise the micropores (<2 nm) and mesopores (2–50 nm). For ultramicropores (<0.7 nm), we perform CO₂ physisorption at 273 K with the Dubinin–Radushkevich (DR) method. For macroporosity and interparticle voids, we perform mercury intrusion porosimetry (up to 600 MPa) to obtain the bulk density, the pore throat distribution, and the skeletal density. The micropore volume and the external surface area are obtained from the t‑plot. These textural parameters are directly correlated with the breakthrough capacity and the mass‑transfer kinetics.
We evaluate the breakthrough sulfur capacity using a custom‑built fixed‑bed reactor system that simulates industrial flue gas or biogas conditions. The system precisely controls the temperature (25–300 °C), the pressure (1–10 bar), the gas flow rate, and the inlet concentration of SO₂ (100–5000 ppm) or H₂S (50–2000 ppm), along with O₂, H₂O, and CO₂. The effluent concentration is monitored continuously by an online UV‑fluorescence analyzer (for SO₂) or by a gas chromatograph with a sulfur‑specific detector (GC‑SCD). From the breakthrough curves, we derive the breakthrough capacity (at 5% and 10% penetration), the saturation capacity, the mass transfer zone (MTZ) length, and the utilisation efficiency of the active sites. We also perform multi‑cycle tests (adsorption – regeneration – re‑adsorption) to evaluate the regenerability and the capacity decay. For VOC removal, we use toluene or acetone as model compounds with online GC‑FID detection.
We measure the single‑pellet crush strength using a precision universal tester (load cell accuracy: ±0.1 N) on at least 30 individual particles, reporting the mean and the distribution. The attrition resistance is evaluated by the tumble drum method (ASTM D4058) and by the fluidised bed attrition test (ASTM D5757), providing the attrition index and the fines generation percentage. The particle size distribution is determined by mechanical sieving and by laser diffraction (0.1–3500 µm). These mechanical properties are critical for predicting the pressure drop, the bed packing behaviour, and the dust generation during long‑term operation and pneumatic transport.
We perform simultaneous Thermogravimetric Analysis (TGA) and differential scanning calorimetry (DSC) from 25 °C to 1000 °C under inert and oxidizing atmospheres, with evolved gas analysis by mass spectrometry (MS) to monitor the release of CO, CO₂, H₂O, SO₂, and volatile organic compounds. The ignition temperature is determined by a standardised test (ASTM D3466) using a TGA method with a defined heating rate in an air flow, reporting the temperature at which the exothermic oxidation commences. The TGA curve also reveals the moisture content, the volatile matter, the fixed carbon, and the ash content. We also perform cyclic thermal regeneration tests to determine the regeneration efficiency and the energy consumption per cycle, and we re‑characterise the regenerated material by BET and breakthrough capacity to assess the structural integrity.
We characterise the surface basicity by temperature‑programmed desorption of CO₂ (CO₂‑TPD), resolving the weak, medium, and strong basic sites. The surface oxygen‑containing functional groups (carboxyl, phenolic, lactone, carbonyl, and basic sites) are quantified by the Boehm titration method. Diffuse reflectance infrared Fourier transform spectroscopy (DRIFTS) is used to identify the surface hydroxyl and carbonyl groups. The point of zero charge (pHPZC) is determined by the potentiometric mass titration method. These surface chemistry parameters are essential for predicting the adsorption of polar acidic gases and for optimising the activation conditions to enhance the chemisorption capacity.
We determine the major and trace element composition (Si, Al, Fe, Ca, Mg, Na, K, Ti, Mn, and heavy metals: Pb, Cd, As, Hg, Cr, Ni, Cu, Zn) by X‑ray fluorescence (XRF) on fused beads and by inductively coupled plasma mass spectrometry (ICP‑MS) after acid digestion, with detection limits in the sub‑ppb range. The ash content is determined by the loss on ignition at 800 °C. The mineral phases (e.g., quartz, aluminosilicates, pyrite) are identified by powder X‑ray diffraction (XRD) with Rietveld refinement. The ash composition and the trace metals are correlated with the catalytic activity (e.g., iron promotes SO₂ oxidation) and the environmental safety (e.g., mercury content).
We measure the moisture content by Karl Fischer coulometric titration (detection limit: 0.01%) and by loss on drying at 105 °C (ASTM D2867). The volatile matter (including residual organic compounds from the activation process) is determined by TGA at 900 °C under nitrogen. The moisture and volatile content are critical for preventing the caking, for predicting the combustion behaviour, and for ensuring the reproducibility of the activation process.
We examine the particle morphology and the surface texture by field‑emission scanning electron microscopy (FE‑SEM) with EDS elemental mapping, and by transmission electron microscopy (TEM) for the nanoporous structure. The particle size and shape are also quantified by laser diffraction and by image analysis. These morphological features influence the packing density, the flowability, and the accessibility of the internal pore network.
We perform batch leaching tests in deionized water and in acidic (pH 4) and alkaline (pH 10) solutions, following EPA Method 1311 (TCLP) or custom protocols. The leachate is analysed for heavy metals by ICP‑MS and for anions (chloride, sulfate, fluoride) by ion chromatography (IC). We also measure the total dissolved solids (TDS) and the pH of the extract. These data are essential for assessing the environmental compatibility of the spent adsorbent and for compliance with disposal regulations.
1. Integrated Dynamic and Physicochemical Platform: We uniquely combine real‑time breakthrough testing (SO₂, H₂S, VOCs) with detailed textural (BET, mercury porosimetry), chemical (surface basicity, Boehm, XRF, ICP‑MS), thermal (TGA‑DSC‑MS), and mechanical (crush strength, attrition) analyses in a single workflow. This integration enables us to correlate the pore architecture with the breakthrough curve, the surface basicity with the sulfur capacity, and the mechanical strength with the operational longevity – providing a complete fitness‑for‑purpose assessment that is rarely available from standard testing services.
2. Expertise in Coal‑Based Carbonaceous Materials and Gas Cleaning: Our team has extensive experience with activated carbons, semi‑cokes, and char materials. We have developed customised sample preparation and degassing protocols to handle the high ash content and the variable pore structure of semi‑coke. Our inter‑laboratory reproducibility for key parameters (BET, sulfur capacity, crush strength) is within 2‑3% RSD, validated on over 150 commercial semi‑coke products.
3. Regulatory‑Ready Quality and Full Traceability: Our facility is accredited under ISO/IEC 17025:2017 for BET, mercury porosimetry, TGA, crush strength, and breakthrough testing. We use NIST‑traceable gas standards and certified reference materials. All measurement uncertainties are reported with expanded uncertainties (k=2) typically <2% for surface area, <3% for breakthrough capacity, and <5% for mechanical properties, ensuring the data are defensible in quality audits, regulatory submissions, and customer certifications.
4. Consultative Partnership and Application Support: Each project is led by a senior carbon scientist with deep knowledge of gas‑phase adsorption. We provide interpretative reports that not only present the analytical results but also offer a benchmarking summary against competitor products and a process optimisation guide – recommending the optimal operating conditions (temperature, flow rate, bed depth) and the regeneration parameters. We also assist in diagnosing field failures (e.g., capacity loss due to pore blockage or sulfate formation) and in designing corrective actions. We support co‑authorship for technical publications and assist in drafting the technical dossiers for product approval.
Our final comprehensive report includes: (a) BET surface area, micropore and mesopore volumes, pore size distribution (NLDFT, BJH), and mercury porosimetry data; (b) breakthrough and saturation capacities for SO₂ and/or H₂S, with MTZ length and utilisation efficiency; (c) single‑particle crush strength, attrition index, and particle size distribution (D10, D50, D90); (d) ignition temperature, thermal stability profile (TGA‑DSC‑MS), and regeneration efficiency; (e) surface basicity (CO₂‑TPD), Boehm titration results, DRIFTS spectra, and pHPZC; (f) elemental composition (XRF) and trace metal profile (ICP‑MS) with ash analysis; (g) moisture and volatile matter; (h) SEM and TEM images with EDS maps; (i) leachate chemistry and environmental compliance assessment; (j) a benchmarking summary comparing your ASC with reference materials and competitor products; and (k) a process optimisation guide with recommended operating parameters and regeneration schedules. All raw data (breakthrough logs, isotherms, diffractograms, spectra, thermograms, and images) are supplied in open, machine‑readable formats (CIF, JCAMP‑DX, .csv, .tiff, .mzML) for independent verification and long‑term data archiving.
We also offer subscription‑based quality surveillance programs for regular batch inspection, with trend analysis and statistical process control (SPC) charts. Our secure client portal provides 24/7 access to project data and direct communication with our technical experts.
Activated semi‑coke adsorbents are a cost‑effective and robust solution for industrial gas cleaning, but their performance and reliability depend on a thorough understanding of their physical, chemical, thermal, and mechanical properties. Our testing service provides that understanding – integrating advanced dynamic testing, detailed textural and chemical characterisation, mechanical durability assessment, and safety screening with expert interpretation. By choosing our laboratory, you gain a trusted partner that ensures your ASC meets the most stringent specifications for desulfurization, denitrification, and mercury removal, enabling you to achieve consistent performance, extended service life, and regulatory compliance. Contact our expert team today to design a customized testing protocol – we are committed to advancing your air purification technology with unparalleled analytical depth and scientific rigor.
Beijing ZKGX Institute of Science and Technology , combining applied research with technological transformation. It has evolved into a comprehensive research institute characterized primarily by a "task-driven disciplines" approach. Approved by relevant authorities, it currently operates as a third-party analytical testing technical service provider. Its affiliated laboratory facilities hold certifications including CMA and CNAS, possess an Experimental Animal Use License, and have achieved triple certification for ISO9001 Quality Management System, ISO14001 Environmental Management System, and ISO45001 Occupational Health and Safety Management System.