IS 9178 Part 1 (1979) establishes the general requirements and load assessment criteria for the design of steel bins used to store bulk materials, including granular and powdery substances. It provides engineers with methodologies to evaluate pressures and loads acting on bin walls and bottoms during filling, emptying, and special conditions such as pneumatic emptying or eccentric outlets. This standard is essential for structural and design engineers involved in the planning and construction of steel storage bins in industries like power plants, cement, fertilizers, and grain storage.
Overview
IS 9178 Part 1 (1979) establishes the general requirements and load assessment criteria for the design of steel bins used to store bulk materials, including granular and powdery substances. It provides engineers with methodologies to evaluate pressures and loads acting on bin walls and bottoms during filling, emptying, and special conditions such as pneumatic emptying or eccentric outlets. This standard is essential for structural and design engineers involved in the planning and construction of steel storage bins in industries like power plants, cement, fertilizers, and grain storage.
Audience
Contents
Structure
Scope:
IS 9178 Part 1 covers design parameters and material handling systems for bulk storage structures, focusing on bulk material characteristics, pressures, and handling.
| Material Characteristic | Class |
|---|---|
| Very fine (<100 micron) | A |
| Fine (<3 mm) | B |
| Granular (<12 mm) | C |
| Lumpy (>12 mm) | D |
| Irregular (fibrous) | H |
| Flowability: Very free flowing | 1 |
| Flowability: Free flowing | 2 |
| Flowability: Sluggish | 3 |
| Abrasiveness: Non-abrasive | 6 |
| Abrasiveness: Mild | 7 |
| Abrasiveness: Very abrasive | 8 |
| Material | Bulk Density (kg/m³) | Class | Angle of Internal Friction (°) |
|---|---|---|---|
| Ammonium nitrate | 720-1000 | B27NLS | 25 |
| Coal, dry (12 mm under) | 560-640 | C37 | 40 |
| Cement | 1350 | - | 25 |
| Sand, bank, dry | 1440-1760 | B28 | 30 |
| Sulphur, crushed (12 mm) | 800-960 | C26S | 30-45 |
Use these values for design pressures and flow analysis.
[ P = W \times H \times K ]
IS 9178 Part 1 (1979) - Key Definitions, Formulas & Tables
| Material | Bulk Density W (kg/m³) | Angle of Internal Friction ϕ (°) |
|---|---|---|
| Ammonium nitrate | 720 - 1000 | 25 |
| Coal, anthracite | 830 - 960 | 30 - 45 |
| Cement | 1350 | 25 |
| Gypsum, calcined | 880 - 960 | 40 |
| Sand, bank, dry | 1440 - 1760 | 30 |
| Sulphur, crushed | 800 - 960 | 30 - 45 |
[ A = \tan \delta = \frac{P_w}{P_h} ]
IS 9178 Part 1 - Key Notations and Tables Summary
| Symbol | Meaning |
|---|---|
| A | Horizontal cross-sectional area at depth z |
| a, b | Sides of rectangular bin (a = shorter, b = longer) |
| D | Internal diameter of circular bin |
| d | Max inscribed circle diameter in bin |
| h | Height of bin |
| Pa | Air pressure for pneumatic emptying |
| Ph, Pv, Pw | Horizontal, vertical, and wall friction pressures |
| Pnl | Pressure on wall for concentric eccentric opening |
| S | Bottom diameter of insert |
| U | Perimeter of cross-section at depth z |
| W | Bulk density of stored material (kg/m³) |
| z | Depth below leveled surface of max fill |
| δ | Wall friction angle |
| θ | Hopper wall slope angle |
| φ | Internal friction angle (angle of repose) |
| α, β | Wall friction coefficients during filling/emptying |
| A, Mf, Me | Pressure ratios |
Used for pressure distribution calculations in bins.
| z/z0 | 1 - e^(-z/z0) |
|---|---|
| 0.01 | 0.010 |
| 0.05 | 0.049 |
| 0.10 | 0.090 |
| 0.20 | 0.181 |
| 0.50 | 0.393 |
| 1.00 | 0.632 |
| 2.00 | 0.865 |
(Values interpolate for design use)
Typical bulk densities (W) and minimum internal friction angles (φ) for common materials:
| Material | Bulk Density W (kg/m³) | φ (°) |
|---|---|---|
| Ammonium nitrate | 720 - 1000 | 25 |
| Ashes, coal, dry | 560 - 640 | 38 - 40 |
| Cement | 1350 | 25 |
IS 9178 Part 1 - General Requirements Summary
| Material | Bulk Density (W) | Angle of Internal Friction (φ) |
|---|---|---|
| Ammonium nitrate | 720 - 1000 | 25° |
| Coal, dry, 12 mm under | 560 - 640 | 40° |
| Cement | 1350 | 25° |
| Sand, dry | 1440 - 1760 | 30° |
| Sulphur, crushed | 800 - 960 | 30-45° |
[ P = W \times H \times K ]
graph TD
A[Bulk Material] -->|Weight (W)| B[Vertical Load]
B --> C[Bin Wall]
A -->|Friction (φ)| D[Horizontal Load]
D --> C
C --> E[Structural
IS 9178 Part 1: Design Parameters Summary
| Material | Bulk Density (kg/m³) | Class | Angle of Internal Friction (°) |
|---|---|---|---|
| Ammonium nitrate | 720 - 1000 | B27NLS | 25 |
| Coal, dry (<12 mm) | 560 - 640 | C37 | 40 |
| Cement | 1350 | - | 25 |
| Limestone, crushed | 1360 - 1440 | D27 | 30 - 45 |
| Sand, bank, dry | 1440 - 1760 | B28 | 30 |
| Parameter | Value |
|---|---|
| 0.01 | 0.56 |
| 0.10 | 0.65 |
| 1.00 | 0.632 |
| 2.00 | 0.865 |
| 3.00 | 0 |
IS 9178 Part 1: Assessment of Loads - Key Points
| Load Type | Granular Material | Powdery Material |
|---|---|---|
| Pv (Vertical Pressure) | Filling | Filling |
| Ph (Horizontal Pressure) | Emptying | Emptying |
| Pw (Wall Pressure) | Emptying or Filling (depends) | Filling = Emptying |
| Condition | Granular Material | Powdery Material |
|---|---|---|
| Vertical Pressure | Filling | Filling |
| Horizontal Pressure | Emptying | Emptying |
| Wall Pressure | Emptying/Filling | Filling=Emptying |
flowchart TD
A[Material Type] --> B{Granular}
A --> C{Powdery}
B --> D[Filling
IS 9178 Part 1: Flow Correction and Emptying Devices
| Parameter | Symbol | Typical Value/Range |
|---|---|---|
| Bulk density | γ | 15 - 20 kN/m³ |
| Internal friction angle | φ | 25° - 40° |
| Wall friction angle | δ | 15° - 30° |
| Flow correction factor | k | 0.8 - 1.0 (depending on insert size) |
[ P_e = \gamma \cdot H \cdot k ]
flowchart TD
A[Bin] -->|Large Insert| B[Transition Zone]
B --> C[Hopper]
C -->|Small Insert| D[Hopper Outlet]
Summary: Use inserts to control flow pattern and reduce excess pressure. Refer to IS 9178 Tables 2 & 3 for design parameters and apply correction factors in pressure calculations. Special unloading devices negate excess pressure concerns by layer
IS 9178 Part 1 - Material Handling System: Key Points
| Material Example | Bulk Density (kg/m³) | Angle of Internal Friction (°) |
|---|---|---|
| Ammonium nitrate | 720 - 1000 | 25 |
| Coal, dry (12 mm) | 560 - 640 | 40 |
| Cement | 1350 | 25 |
| Sand, bank, dry | 1440 - 1760 | 30 |
[ P = W \times H \times K_a ] Where:
flowchart TD
A[Material Handling System] --> B[Belt Conveyor]
A --> C[Bucket Elevator]
A --> D[Screw Conveyor]
A --> E[Pneumatic Elevator]
B --> F[Load on Bin Cover]
C -->
Pressure Variation Along Bin Depth (IS 9178 Part 1, Clause 6.2.1.3)
The pressure at any depth ( z ) in the bin is given by:
[ P_i(z) = (P_i)_{\max} \left( 1 - 2^{-\frac{z}{Z_i}} \right) ]
Characteristic Depth ( Z_i ):
| Condition | Expression |
|---|---|
| Filling | ( Z_{or} = \frac{R}{u_r} dt ) |
| Emptying | ( Z_{oe} = R_i p_e d_e ) |
(Refer to Appendix A for values of ( 1 - 2^{-z/Z_i} ) and use linear interpolation for intermediate values.)
Bin Bottom Pressure Reduction (Clause 6.7.1):
Horizontal pressure during emptying reduces linearly from emptying pressure at height ( \min(1.2d, 0.75h) ) above bin bottom to filling pressure at bin bottom.
Horizontal Pressure Increase due to Air Inlets (Clause 6.6.3.1):
Increase horizontal pressure by inlet air pressure over the height of air inlets; taper linearly to zero at bin top.
Homogenization (Clause 6.3.2):
For powdery materials mixed by compressed air, lateral and vertical pressures depend on the void volume (~40% of bin volume). Use the above formula but pressure should not be less than that calculated by Clause 6.2.1.
graph LR
A[Top of Bin] -->|Pressure decreases| B[Depth z]
B -->|Pressure max at base| C[Bin Bottom]
C -->|Pressure reduction| D[Height min(1.2d,0.75h)]
**Use this formula and guidelines to calculate pressure variation accurately along bin
IS 9178 Part 1: Material Handling Equipment & Layout - Key Points
| Equipment Type | Design Impact | Notes |
|---|---|---|
| Belt Conveyor | Load on bunker cover, supports | Requires openings |
| Bucket Elevator | Vertical load, support structure | Requires cover openings |
| Screw Conveyor | Load on support beams | Consider torque and vibration |
| Pneumatic Elevator | Pressure loads, sealing | Requires airtight design |
| Discharge Devices | Load on bunker columns | Design for operational loads |
flowchart LR
A[Material Handling Equipment] --> B[Belt Conveyor]
A --> C[Bucket Elevator]
A --> D[Screw Conveyor]
A --> E[Pneumatic Elevator]
B & C & D & E --> F[Load on Bunker Structure]
F --> G[Design Considerations]
G --> H[Openings on Cover]
G --> I[Support Beams]
G --> J[Bunker Columns]
Note: Always refer to Appendix B
Frequently Asked
Key Load Cases for Designing Steel Bins as per IS 9178 Part 1:
Normal Filling and Emptying Loads (Clause 6.2.1):
Static Loads from Stored Material:
Load Combinations:
[ \sigma_h = K \sigma_v = K \gamma h ]
Loading diagram...
Note: For detailed design, refer to IS 9178 Part 3 (under preparation) for flow-specific load considerations.
IS 9178 Part 1 addresses pressure variations during filling and emptying of bulk materials as follows:
Normal Filling and Emptying (6.2.1): Base lateral and vertical pressures are calculated using standard pressure schemes (refer to Clause 6.2.1).
Pneumatic Emptying (6.3.4): Air is injected near the bin bottom to fluidize material, increasing lateral and vertical pressures (Ph = Pv). Pressures are calculated per the pressure scheme in Fig. 4, accounting for this fluidization effect.
Homogenization (6.3.2): For bins with powdery materials mixed by compressed air, lateral and vertical pressures depend on the empty volume (~40% of bin volume) in the upper portion. Pressures are calculated using a specific expression but must not be less than those from Clause 6.2.1.
Special Unloading Devices (6.7.2): If only the top layer is withdrawn at a time (layers below remain static), excess pressure during emptying can be ignored.
| Condition | Pressure Consideration | Calculation Reference |
|---|---|---|
| Normal Filling/Emptying | Standard lateral and vertical pressures | Clause 6.2.1 |
| Pneumatic Emptying | Increased pressures due to fluidization (Ph=Pv) | Clause 6.3.4, Fig. 4 |
| Homogenization | Depends on ~40% empty volume, min. as per 6.2.1 | Clause 6.3.2 |
| Special Unloading | Excess pressure ignored if only top layer withdrawn | Clause 6.7.2 |
Loading diagram...
This ensures safe design by accounting for pressure variations due to operational methods.
Design Considerations for Bins with Eccentric Outlets (IS 9178 Part 1)
Summary Table:
| Parameter | Condition to Ignore Eccentricity Effect |
|---|---|
| Eccentricity ( e ) | ( e < \frac{d}{6} ) |
| Bin Height ( h ) | ( h \leq 2d ) |
Loading diagram...
This ensures safe design against asymmetric horizontal pressures due to eccentric emptying.
According to IS 9178 Part 1, granular and powdery materials are classified and treated differently in bin load assessment as follows:
| Load Type | Granular Material | Powdery Material |
|---|---|---|
| Pv (Vertical pressure) | Filling | Filling |
| Ph (Horizontal pressure) | Emptying | Emptying |
| Pw (Wall pressure) | Emptying (finite depth), Filling=Emptying (infinite depth) | Filling=Emptying |
Loading diagram...
This classification guides appropriate design pressures for bin walls and hopper structures.
Impact of Material Handling Systems on Steel Bin Design (IS 9178 Part 1):
| Factor | Effect on Bin Design |
|---|---|
| Handling equipment loads | Additional structural loads |
| Material flow disruption | Need for insert/support design |
| Bin geometry/layout | Optimized for handling efficiency |
Loading diagram...
In brief: Material handling systems directly affect the structural loads and flow conditions, necessitating careful design of bin geometry, inserts, and supports per IS 9178 Part 1.
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