Alum
Alum refers to two closely related aluminum sulfate compounds used in the oil and gas industry: potassium alum (KAl(SO₄)₂·12H₂O, molecular weight 474.4 g/mol), the crystalline double sulfate of potassium and aluminum used in water treatment and textile dyeing since antiquity; and commercial aluminum sulfate (Al₂(SO₄)₃·18H₂O, molecular weight 666.4 g/mol), the hydrated industrial form applied as a coagulant in produced water treatment, as a drilling fluid additive, and as a cement accelerator in low-temperature wellbore cementing. In oilfield usage, "alum" almost always refers to commercial aluminum sulfate rather than potassium alum, because aluminum sulfate is available in large quantities at lower cost and behaves identically in aqueous solution. The fundamental chemistry of both compounds is the same: dissolution releases Al³⁺ ions, which hydrolyze at pH 6 to 8 to form aluminum hydroxide (Al(OH)₃) floc, a gelatinous precipitate with surface area of 200 to 400 m²/g that adsorbs suspended oil droplets, colloidal silica, clay particles, and dissolved organic matter from produced water. In the Western Canada Sedimentary Basin, alum is used in three primary oilfield contexts: (1) produced water treatment at waterflood injection facilities for Cardium, Viking, and Mannville sandstone pools, where suspended solids and residual oil in recycled produced water must be removed before reinjection to prevent injection well plugging; (2) oil sands tailings pond process water treatment, where alum coagulates fine kaolinite and illite clay particles from mature fine tailings (MFT) decant water before it is recycled to primary bitumen extraction; and (3) low-temperature cementing in permafrost zones of northern Alberta and British Columbia, where aluminum sulfate accelerates cement hydration at 2 to 10°C to reduce thickening time and allow drilling to proceed on schedule. Alum doses in produced water treatment range from 50 to 300 mg/L as Al₂(SO₄)₃, selected by jar testing to achieve treated water specifications of oil-in-water below 10 mg/L and total suspended solids below 5 mg/L before reinjection, with pH adjustment to the optimal 6.5 to 7.5 range using NaOH or H₂SO₄ depending on the natural bicarbonate alkalinity of the produced water stream.
Key Takeaways
- Aluminum sulfate coagulates suspended oil and solids in produced water by releasing Al³⁺ ions that hydrolyze to form Al(OH)₃ floc, which adsorbs oil droplets and particles through charge neutralization and sweep flocculation, with the treated water then passing through dissolved air flotation or plate pack separators to meet injection water quality specifications for sandstone waterflood reservoirs: When aluminum sulfate dissolves in produced water at pH 6 to 8, the Al³⁺ ions rapidly form monomeric and polymeric aluminum hydroxide colloids carrying a positive charge that neutralizes the negative surface charge of oil droplets and suspended clay particles (zeta potential shifted from -30 to -50 mV toward zero). The neutralized particles aggregate and are swept into the growing Al(OH)₃ floc gel during slow mixing (30 to 60 rpm, 15 to 30 minutes). Typical alum doses for Cardium and Viking waterflood produced water in central Alberta range from 50 to 200 mg/L, reducing oil-in-water content from 50 to 500 mg/L to below 10 mg/L and suspended solids from 15 to 150 mg/L to below 5 mg/L, meeting the injection water quality standard for 10 to 200 mD sandstone reservoirs. High-salinity Mannville heavy oil produced water (TDS 15,000 to 50,000 mg/L) requires higher doses of 150 to 300 mg/L because dissolved salts compress the electrical double layer and reduce coagulation efficiency at equivalent doses used for lower-salinity Cardium and Viking streams.
- Optimal alum dose for each produced water stream is determined by jar testing at the field laboratory, evaluating multiple doses and pH values to identify the treatment conditions achieving the lowest residual oil-in-water and turbidity at minimum chemical cost, with results translated into continuous-flow operating setpoints at the waterflood battery injection facility: Jar testing for WCSB produced water treatment evaluates alum doses from 25 to 400 mg/L in 500 mL volumes, measuring residual turbidity (NTU), oil-in-water (mg/L by infrared spectroscopy), and dissolved iron after 30 minutes of settling, with pH adjusted using NaOH or H₂SO₄ to maintain the 6.5 to 7.5 optimal window for Al(OH)₃ floc formation. The pH sensitivity of alum is critical: below pH 5.5, Al³⁺ remains soluble and no floc forms; above pH 8.0, the amphoteric Al(OH)₄⁻ aluminate ion forms (no floc), so produced water with high bicarbonate alkalinity (greater than 800 mg CaCO₃/L, common in Belly River and Milk River aquifer water) requires acid addition ahead of the alum injection point. Jar tests for Mannville heavy oil produced water in the Lloydminster area, where oil-in-water concentrations of 200 to 600 mg/L are common, typically determine optimal doses of 150 to 300 mg/L alum plus 3 to 8 mg/L cationic polyacrylamide as a flocculation aid, achieving OIW below 15 mg/L before the water enters the disposal or injection pump header.
- In oil sands operations at Fort McMurray, aluminum sulfate coagulates fine clay particles in process-affected tailings pond water to reduce turbidity before recycling to primary bitumen extraction, supporting AER Directive 085 progressive MFT volume reduction requirements and reducing freshwater intake obligations from the Athabasca River Water Act licence: Mature fine tailings ponds contain kaolinite and illite clay at 0.1 to 20 micron diameter suspended at 200 to 400 g/L, remaining colloidal for years because electrostatic repulsion between negatively charged clay surfaces prevents aggregation. Alum coagulation at 300 to 1,200 mg/L, combined with polyacrylamide flocculation at 20 to 80 mg/L, reduces suspended solids in the turbid decant water layer (5,000 to 15,000 mg/L) to below 500 mg/L for recycle to primary extraction, reducing freshwater intake from the Athabasca River by 20 to 35% per unit of bitumen produced. The AER's Directive 085 compliance reporting requires operators (Syncrude, Suncor, CNRL Horizon, Imperial Oil Kearl) to demonstrate annual reductions in MFT inventory, driving investment in large-scale alum-based coagulation-flocculation systems with capital costs of CAD 15 to 50 million per installation at each mine site, treating 50,000 to 200,000 m³/day of process-affected water.
- Aluminum sulfate accelerates Type G and Class A cement hydration in permafrost cementing at 2 to 10°C by providing aluminate ions that seed calcium aluminate hydrate crystal growth, reducing thickening time from 6 to 12 hours to 2 to 4 hours at near-freezing temperatures, allowing surface and intermediate casing strings to be cemented on schedule without excessive waiting-on-cement delays: In permafrost zones of northern Alberta (Colville Hills, Liard Basin) and British Columbia, static bottomhole temperatures at 100 to 400 m depth are 2 to 8°C, where Type G cement hydration kinetics are so slow that thickening times exceed waiting-on-cement windows before the next casing string can be run. Aluminum sulfate at 0.5 to 2.0% by weight of cement (BWOC) accelerates the tricalcium aluminate (C₃A) and tricalcium silicate (C₃S) reactions by providing additional aluminate reaction sites, reducing thickening time at 4°C from 8 to 12 hours to 2 to 4 hours and compressive strength development from 24 to 48 hours to 10 to 18 hours. Alum accelerator is combined with Class A or Class C cement (higher C₃A content than Class G) and sometimes with calcium chloride at 2% BWOC for maximum acceleration synergy at bottomhole temperatures below 4°C, as specified in cementing programs submitted to the AER or BC Oil and Gas Commission for exploration wells in northern gas fields.
- The principal environmental constraint on alum use in oilfield water treatment is residual dissolved aluminum in treated effluent, which is acutely toxic to freshwater fish above 0.1 mg/L and must meet the Canadian Water Quality Guideline of 0.005 mg/L total Al in any surface discharge, a requirement that drives WCSB operators to use alum in closed-loop produced water reinjection systems rather than discharge-to-surface treatment trains wherever possible: Dissolved Al³⁺ above 0.1 to 0.5 mg/L is acutely toxic to rainbow trout and other salmonids by precipitating Al(OH)₃ on gill surfaces at pH 5.5 to 7.0, causing asphyxiation within 24 to 96 hours, with chronic toxicity at concentrations as low as 0.05 mg/L. Alberta Environment and Parks' Canadian Water Quality Guideline for the Protection of Aquatic Life (CWQG-PAL) specifies 0.005 mg/L total aluminum (5 micrograms per litre) at pH greater than 7, applying to any produced water, process water, or drilling waste discharged to surface watercourses. Because most WCSB waterflood produced water is reinjected rather than discharged, the main alum-related environmental compliance issue arises at oil sands sites with surface discharge permits for treated process water, where operators must demonstrate through continuous monitoring that aluminum concentrations in seepage or overflow reaching the Athabasca River remain below the CWQG-PAL, achieved by maintaining discharge water pH above 7.5 (to keep Al as insoluble Al(OH)₃) and monitoring at licensed tributary entry points under the Alberta Water Act.
Alum in Waterflood Produced Water Treatment Systems
Alum treatment of produced water is integrated into waterflood injection facilities as a continuous-flow process. The produced water handling train at a typical central Alberta Cardium or Viking waterflood battery consists of: free-water knockouts (FWKOs) separating bulk oil from produced water at 30 to 60 minutes residence time, reducing oil-in-water from 5,000 to 50,000 mg/L to 200 to 1,000 mg/L; skim tanks providing additional gravity separation (OIW reduced to 50 to 200 mg/L); alum coagulation tanks where aluminum sulfate plus optional cationic polymer are dosed at controlled pH with 15 to 30 minutes of slow mixing for floc growth; and either dissolved air flotation (DAF) or inclined plate pack separators to remove floc-entrained oil before the water enters the injection pump suction header. The treated water specification for reinjection into 10 to 200 mD Cardium and Viking sandstones is typically OIW below 10 mg/L and total suspended solids below 5 mg/L, set by AER Directive 056 waterflood scheme approval conditions to prevent injection well plugging by oil coating on formation sand grains near the wellbore face.
Fast Facts
The term "alum" derives from the Latin "alumen," applied by Roman writers to the astringent potassium alum mineral (KAl(SO₄)₂·12H₂O) mined at Melos (now Milos, Greece) since at least 1300 BCE for textile dye fixation, wound treatment, and water purification. Commercial aluminum sulfate (Al₂(SO₄)₃) was first produced industrially in England around 1802 by reacting bauxite ore with sulfuric acid, and is today manufactured in Canada from bauxite and kaolin clay, with the Canadian market consuming approximately 120,000 tonnes per year split among municipal drinking water clarification (65%), paper and pulp manufacture (20%), and industrial water treatment including oilfield produced water and oil sands tailings applications (15%). The WCSB oil sands sector is estimated to consume 12,000 to 18,000 tonnes of Al₂(SO₄)₃ per year across tailings pond and process water recycling operations at the four major Athabasca mine sites. The aluminum sulfate price in Western Canada is approximately CAD 320 to 450 per tonne as a 17% Al₂O₃ liquid solution (the standard commercial form for water treatment), representing a chemical cost of CAD 32 to 135 per million litres of produced water treated at typical doses of 100 to 300 mg/L, a modest operating cost compared to the CAD 5,000 to 20,000 per well per year in productivity loss that injection well plugging by suspended solids causes when water treatment is inadequate and waterflood-pattern voidage cannot be maintained.