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Heavy Metal Precipitants

Chemical precipitants for the removal of dissolved heavy metals, including nickel, chromium, copper, zinc, lead, and mercury to comply with PROPER and AMDAL effluent standards.

Wastewater Treatment Effluent Compliance Industrial ETP Hydroxide & Sulfide Precipitation
Primary Chemistries
Hydroxide · Sulfide · Dithiocarbamate · TMT-15
Target Metals
Ni · Cr · Cu · Zn · Pb · Hg · Cd
pH for Precipitation
8.5 – 11.0 (hydroxide); 7.0 – 9.0 (sulfide/DTC)
Process
Precipitation → Coagulation → Sedimentation

Overview

Heavy metals dissolved in industrial wastewater pose significant environmental and regulatory risks. Unlike organic pollutants that can be degraded biologically, heavy metals persist in the environment indefinitely. Indonesian PROPER and AMDAL regulations specify strict discharge limits for heavy metals in industrial effluent; exceeding these limits carries substantial regulatory, financial, and reputational consequences.

Chemical precipitation is the standard and most cost-effective treatment technology for heavy metal removal. The dissolved metal ions are reacted with a precipitant chemical to form insoluble metal compounds such as hydroxides, sulfides, or organosulfur complexes, which are then removed from the wastewater by coagulation, flocculation, and sedimentation or filtration. The correct precipitant selection depends on the metals present, the required effluent limits, the wastewater matrix (pH, temperature, competing ions, chelants), and downstream sludge management considerations.

Chelated metals: Some industrial processes (electroplating, metal finishing, printed circuit board manufacturing) use chelating agents (EDTA, citrate, gluconate) that form soluble complexes with heavy metals and prevent them from precipitating at normal hydroxide precipitation pH. For chelated metal streams, conventional lime/NaOH precipitation will not achieve discharge limits. Organic sulfide precipitants (TMT-15, sodium dimethyldithiocarbamate) or advanced oxidation pretreatment to break down chelants is required. Always characterise the wastewater matrix before selecting a precipitant.

Precipitant Types

Hydrated Lime / Caustic Soda
Hydroxide precipitation is the simplest and most widely used method. Raising pH to 9.0–11.0 causes most metals (Cr, Zn, Cu, Ni, Cd, Pb) to precipitate as insoluble metal hydroxides. Cost effective for straightforward metal streams without chelants. Different metals have different optimum precipitation pH. A single-pH step may not simultaneously minimise all metals; staged precipitation at multiple pH set points achieves better results for mixed-metal streams.
TMT-15 (Trisodium Trimercapto-s-triazine)
Organic sulfur precipitant that forms extremely insoluble metal-TMT complexes. Effective for mercury, lead, and cadmium at very low final concentrations. This approach surpasses hydroxide precipitation in achieving near-discharge-limit residuals. Also breaks through metal-chelant complexes. Effective at neutral to slightly alkaline pH, reducing the need for high pH adjustment. Used as a polishing reagent after hydroxide pre-precipitation, or as the primary precipitant for mercury-containing streams.
Sodium Dimethyldithiocarbamate (SDDC)
Dithiocarbamate precipitant. Widely used for copper, nickel, zinc, lead, and cadmium. Reacts rapidly with dissolved metals to form insoluble dithiocarbamate complexes that are then removed by coagulation and sedimentation. Effective for chelated metal streams where hydroxide precipitation fails. Available in liquid form for direct metered dosing.
Sodium Sulfide / Ferrous Sulfate
Inorganic sulfide precipitation produces metal sulfides, which are generally less soluble than the corresponding hydroxides, which is beneficial for achieving very low mercury and cadmium residuals. Ferrous sulfate is specifically used for hexavalent chromium (Cr⁶⁺) reduction to trivalent Cr³⁺ under acidic conditions before hydroxide precipitation; Cr⁶⁺ does not precipitate directly as a hydroxide.

Applications

Application Key Metals Recommended Treatment
Refinery wastewater, catalyst fines Ni, V, Mo (from spent catalyst) Hydroxide precipitation at pH 9.5–10.5; coagulation with ferric salt for final polishing
Petrochemical plant ETP Cr, Zn, Cu (from heat exchangers, additives) Cr⁶⁺ reduction with FeSO₄ first; then hydroxide precipitation; SDDC for chelated fractions
LNG plant produced water Hg (from natural gas condensate) Mercury is present in some Indonesian gas fields; TMT-15 achieves sub-µg/L mercury levels required for AMDAL discharge compliance
Mining / mineral processing Pb, Cd, As, Zn Hydroxide + sulfide polishing for arsenic; TMT-15 for Pb/Cd if chelants present
Metal surface treatment / electroplating Cr, Ni, Cu, Zn, Cd (chelated) Cr⁶⁺ reduction; SDDC or TMT-15 for chelated metals; staged precipitation at different pH set points for mixed-metal baths
Battery and electronics manufacturing Ni, Co, Li, Cu TMT-15 or SDDC preferred for complex metal matrices; hydroxide pre-treatment reduces reagent cost

Petrochemical & LNG Applications

Heavy metal contamination in wastewater is a relevant and often overlooked challenge at upstream oil & gas, petrochemical, and LNG operations. While these industries are not "metal industries" in the conventional sense, their processes generate metal-contaminated streams through multiple mechanisms.

In refineries, crude oil contains naturally occurring metals particularly vanadium and nickel in heavy crude fractions that concentrate in the catalyst and in certain process streams. The effluent treatment plant receives wastewater containing catalyst fines, spent caustic solutions, and cooling water blowdown that may contain elevated nickel, vanadium, chromium (from stainless steel corrosion), zinc (from galvanised equipment), and copper (from heat exchanger corrosion). Meeting PROPER and AMDAL metal discharge limits requires a dedicated precipitation step in the ETP.

In LNG operations, mercury is a well-known and critical concern. Indonesian natural gas from several fields contains significant dissolved mercury that concentrates in LNG condensate and process condensate streams. Before these condensate streams can be treated and discharged, mercury must be removed to sub-nanogram per litre levels to comply with discharge limits and to protect downstream equipment (LNG heat exchangers, aluminium cold boxes are highly susceptible to liquid metal embrittlement by mercury). TMT-15 precipitation combined with activated carbon adsorption is the standard treatment train for mercury-containing produced water at LNG sites.

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