Ejector pumps are used for drawing-in (pumping), thrusting and transport of all types of liquids, emulsions and suspensions. Pumped and drawn-in liquids can contain gases (air, methane, carbon dioxide etc) and un-dissolved solid grains and pieces of material of different origin and size.

They are used for performing a series of different operations in many fields (industry, construction, waterpower engineering, mining etc.).

Depending on the type of driving fluid they are divided into:

• ejector hydro pumps (liquid-liquid)
• ejector gas pumps (gas-liquid)
• ejector vapor pumps (vapor-liquid)

1.1 1.1 Ejector hydro pumps (liquid-liquid)

A liquid (most often water) is used as the driving fluid in these pumps. These pumps are widely applied in many fields: for small and large flows (from several l/h to several thousand m³/h), for low and high output pressures (from minimal to > 20 bar), for low and high temperatures, for pumping water from great depths (depths greater than 500 m), for pumping (drawing in) and thrusting liquid with mechanical admixtures of different sizes and origin (see ejector hydro-transport), for pumping (drawing-in) liquid that contain gases, for increasing pumping-in heights of other pumps, for preventing pump cavitation, for transport of warm liquids, for pumping-in and thrusting acid, alkaline and other chemical liquids, emulsions and suspensions with different concentrations and compositions, for performing chemical reactions and other special and individual applications.

Q₁, Q₂ i Q₃ – volume flow in (m³/s) or (m³/h),
r₁, r₂ i r₃ – density in (kg/m³),
p₁, p₂, i p₃ – pressure in (bar), recommended in (bar_aps)

Index 1 denotes the driving fluid entering the ejector, index 2 the drawn-in liquid at the ejector input and index 3 denotes a mixture of driving fluid and drawn-in liquid at the ejector output

Size	Max. flow Q3 (kg/h)	Attachments DN			Dimension (mm)
		A	B	C	a	b	c
1	1200	20	20	20	40	80	150
2	3500	25	20	32	60	85	270
3	6000	32	25	40	65	100	350
4	12000	40	32	50	70	115	410
5	24000	50	40	65	80	125	480
6	32000	65	40	65	80	125	480
7	40000	65	50	80	80	125	530
8	70000	80	65	100	115	135	730
9	100000	100	80	125	150	165	950

Ejectors are produced with flanges, a threaded fastener and attachments for connecting with rubber or plastic tubes.

When ordering an ejector the following data needs to be given:

• density r₁and r₂ in (kg/m³),
• mass flow m₁ and m₂ or at least one of them in kg/s or kg/h or volume flow Q₁ and Q₂ or at least of them in m³/s or m³/h,
• of the three pressures p₁, p₂ and p₃ two must be set (bar or bar_abs),
• if all three pressures are set than only one mass or volume flow can be set (see figure 1 and 1a).

Example 1.1

Data: The pumped water has a flow of m₂=12.4 t/h, density r₂=1.2 t/m³, pressure p₂=1.2 bar_abs (the ejector is set 2 m below the level of the pumped liquid). The driving liquid has a flow of m₁=20 t/h and density r₁=1 t/m³. The pressure required at the ejector output p₃=2.5 bar_abs. The pressure of the driving liquid p₁ needs to be determined.

Solution: for m = m₂/m₁=12,4/20 = 0,62 and r₂/r =1,2/1=1,2

From the diagram one can read y = 0,305 and h = 0,24.

p₁ = p₂ + (p₃ – p₂) / y =1,2 + (2,5 –1,2) / 0,31 = 5,4 bar_aps (4,4 bar)

Example 1.2

All data is the same as in example 1.1 only the ejector is placed 2 m above the pumped liquid level i.e. the pumped water pressure at the ejector input is p₂=0.8 bar_abs (0.2 bar vacuum).

Solution: for m = 0,62; r₂/r =1,2, and for y = 0,305 the required driving liquid pressure is

p₁ = p₂+ (p₃ – p₂) / y = 0,8 + (2,5 – 0,8) / 0,31 = 6,28 bar_aps (5,28 bar)

The utilization coefficient is the same as in example 1.1 h = 0,24.

m = m2/m1(kgsunctioned liquid /kgdriving liquid)

Figure 1.2 Variants for pump and ejector connection

Figure 1.3 Ejector transport of dirty and muddy liquids