Sulfuric Acid (H2SO4 10% – 98%) Specific Gravity, Concentration (% w/w) & Baume (°Be) Lookup Table with Safe Dilution Rules

Sulfuric Acid (H2SO4 10% – 98%) Specific Gravity, Concentration (% w/w) & Baume (°Be) Lookup Table with Safe Dilution Rules
Table of contents

Across industrial operations utilizing Sulfuric Acid H₂SO₄ 98%—ranging from alkaline textile effluent neutralization (pH 10.5–12.0), lead-acid battery electrolyte preparation, and hot-rolled steel pickling to cation-exchange resin regeneration—accurately converting between Specific Gravity (d, g/cm³), Baume degrees (°Be), and mass percentage (% w/w) is essential. Because diluting H₂SO₄ 98% (d = 1.84 g/cm³, 66 °Be) releases 872 kJ of hydration heat per kilogram of pure acid, engineers must perform mass-based dilution calculations and strictly enforce the “Acid Slowly Into Cold Water” protocol in heat-resistant PP / Vinyl Ester FRP vessels.

3-tier IBC rack storage at Loc Thien Chemical warehouse


1. Standard Lookup Table: Specific Gravity (g/cm³), Baume (°Be) & g/L of H₂SO₄ (at 20 °C)

  • Specific Gravity to Baume Conversion: °Be = 145 - (145 ÷ d) and d = 145 ÷ (145 - °Be)
  • Active H₂SO₄ per Liter (g/L): C (g/L) = d (g/cm³) × C (% w/w) × 10

Table 1: Engineering Reference Table for Sulfuric Acid Solutions (5% to 98% w/w at 20 °C)

Mass Concentration (% w/w H₂SO₄)Specific Gravity at 20 °C (d, g/cm³)Baume Degree (°Be)Pure H₂SO₄ per Liter (g/L)Molarity (mol/L)Freezing Point (°C)Primary Industrial Application
5.0%1.03174.5 °Be51.6 g/L0.53 M-1.9 °CCation-exchange resin regeneration (4%–6%), RO membrane descaling.
10.0%1.06619.0 °Be106.6 g/L1.09 M-4.6 °CAutomated pH neutralization of alkaline textile dyeing effluent.
15.0%1.102013.4 °Be165.3 g/L1.69 M-8.6 °CHot-rolled carbon steel pickling baths at 60–80 °C.
20.0%1.139417.7 °Be227.9 g/L2.32 M-13.9 °CAluminum anodizing electrolyte (18%–22% w/w) for Al₂O₃ films.
30.0%1.218526.0 °Be365.6 g/L3.73 M-35.6 °CUncharged battery filling acid / intermediate process acid.
35.0%1.259929.9 °Be441.0 g/L4.50 M-56.6 °CStandard charged lead-acid battery electrolyte (d = 1.26–1.28).
40.0%1.302833.7 °Be521.1 g/L5.31 M-36.0 °CSulfate salt synthesis (CuSO₄, ZnSO₄, Al₂(SO₄)₃).
50.0%1.395141.1 °Be697.6 g/L7.11 M-32.0 °CAmmonia (NH₃) wet scrubber liquor producing (NH₄)₂SO₄.
60.0%1.498348.2 °Be899.0 g/L9.17 M-39.5 °CSuperphosphate fertilizer digestion from apatite ore.
70.0%1.610555.0 °Be1,127.4 g/L11.49 M-39.0 °CChlorine gas (Cl₂) drying towers, chemical synthesis.
80.0%1.727260.9 °Be1,381.8 g/L14.09 M+4.5 °CCaution: Elevated freezing point (+4.5 °C to +8.5 °C at 84%).
93.0%1.827965.7 °Be1,700.0 g/L17.33 M-29.5 °CLow-freezing winter storage grade (-29.5 °C).
98.0%1.836166.0 °Be1,799.4 g/L18.35 M+3.0 °CStandard Commercial Concentrated Sulfuric Acid (66 °Be).

2. Mass-Balance Dilution Table & Adiabatic Temperature Rise (ΔH = -85.5 kJ/mol)

To prepare 1,000 L (mass M₂ = 1,000 × d₂ kg) of target concentration C₂ (% w/w) from commercial H₂SO₄ 98% (d₁ = 1.836 kg/L) and clean water (d₀ = 1.000 kg/L):

  • Required Mass of H₂SO₄ 98% (m₁, kg): m₁ = M₂ × (C₂ ÷ 98.0)
  • Required Volume of Cold Water Added First (V_water, L): V_water = M₂ - m₁

Table 2: Recipe to Prepare 1,000 Liters (1 m³) of Dilute H₂SO₄ from H₂SO₄ 98% & Adiabatic Heat Rise

Target Concentration (% w/w)Target Density (d₂, kg/L)Total Mass of 1,000 L Solution (kg)Volume of Cold Water Filled First (L)Mass of H₂SO₄ 98% Poured Slowly (kg)Equivalent Volume of H₂SO₄ 98% (L)Adiabatic Temperature Rise Without Cooling (ΔT, °C)
5% Solution1.0321,032 kg979.3 L52.7 kg28.7 L+11.2 °C (Safe)
10% Solution1.0661,066 kg957.2 L108.8 kg59.3 L+23.5 °C (Warm ~48 °C)
20% Solution1.1391,139 kg906.6 L232.4 kg126.6 L+51.8 °C (Hot ~77 °C)
30% Solution1.2191,219 kg845.8 L373.2 kg203.3 L+85.4 °C (Boils > 105 °C!)
36% Battery Acid1.2681,268 kg802.2 L465.8 kg253.7 L+107.0 °C (Cooling Mandatory!)
50% Solution1.3951,395 kg683.3 L711.7 kg387.6 L+148.0 °C (Heat Exchanger Required!)

3. Five-Step Safe Dilution SOP (Always Pour Acid Into Water)

  1. Verify Tank Material: Use thick PP, Vinyl Ester FRP, or PTFE-lined steel (never dilute H₂SO₄ inside unlined carbon steel or thin HDPE tanks, which soften above 80 °C).
  2. Fill 100% of the Required Cold Water First: Start the mechanical agitator (60–120 rpm) before opening the acid valve.
  3. Meter Concentrated H₂SO₄ 98% Slowly into the Agitated Water Vortex: Never dump water onto concentrated acid.
  4. Interlock Bath Temperature at T ≤ 55–60 °C: Pause acid feed if temperature approaches 60 °C and allow cooling below 40 °C.
  5. Enforce Full Acid PPE & Eyewash Readiness: Face shield, acid goggles, Neoprene/Butyl gloves, PVC apron, and an operational emergency shower within 10 meters.

ZDHC compliant IBC storage at Loc Thien Chemical warehouse


4. ZDHC MRSL v3.1 Level 1 Certified Sulfuric Acid H₂SO₄ 98% Supply by Loc Thien Chemical

Loc Thien Investment Development Co., Ltd. (LOC THIEN INVESTMENT DEVELOPMENT COMPANY LIMITED — Tax ID: 0313650856) is a specialized commercial supplier and distributor of industrial chemicals in Vietnam:

  1. Official ZDHC MRSL Version 3.1 Conformance Level 1 Credential: H₂SO₄ (Sulfuric Acid) supplied by Loc Thien holds Conformance Summary Report (CSR) and Analytical Test Report No. 248162921-01 (issued 22/10/2024) by TÜV Rheinland Vietnam.
  2. 6 Strategic Warehouses (3,000+ tons/month, 5–30-ton tanker fleet): Ba Ria - Vung Tau (Phu My 1 IP), Dong Nai (Long Thanh IP), Binh Duong (Di An City), Da Nang (Hoa Khanh IP), Can Tho (Tra Noc IP), and Bac Ninh (Tien Son IP). Legal Headquarters: 452/6B Tinh Lo 10, Binh Tri Dong Ward, Binh Tan District, Ho Chi Minh City.
  3. Quotation & Delivery SLA: Technical quotation within 15 minutes; delivery within 4 hours in inner HCMC, 24–48 hours across Southern & Mekong Delta industrial zones, and 2–3 days in Northern & Central Vietnam. Contact hotline 0979 891 929 for detailed delivery procedures.
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