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Sundyne Pumps at Maxam-Chirchiq JSS Carbamide Plant

2002

Since 2002 company ENCE GmbH renders engineering services and carries out integration of the pumps to existing lines at Maxam-Chirchiq JSS.

Our company supplied 38 high-speed single-stage centrifugal pumps of LMV series and auxiliaries for Carbamide production plant. Piston pumps, which operated the plant, were morally and physically outdated. Wear of equipment resulted in gas-polluted air, oil leakage and low efficiency of the plant. Our experts made replacing of all piston pumps to Sundyne high-speed pumps. The system of control and regulation had been changed also. Such modernization was carried out at the chemical manufacturing for the first time.

In the carbamide plant were installed and set up pumps of series LMV-341 Z, LMV-322, LMV-806. In particular, we applied a unique consecutive installation of two pumps LMV-341Z for handling of ammonia and carbamate solution with outlet pressure 200 bar and flow rate 40 m³/h.

In 2002, the group of mechanics of the carbamide plant had an internship at a Sundyne factory in Dijon, France.

Maxam-Chirchiq JSS is one of the largest producers of mineral fertilizers in Uzbekistan. It produces ammonia, urea (carbamide), ammonium nitrate, ammonium sulfate, mixed nitrogen-phosphorus fertilizers, urea-ammonia mixture, ammonium carbonates, nitric acid, amino-formaldehyde resin, carbamide resin, ammonia synthesis catalysts, carbon oxide conversion catalysts, nickel and chromia-alumina catalysts.

Total upgrades:

  • 1. Despite the fact that the centrifugal pumps have 10-15% lower efficiency than piston pumps, centrifugal pumps have a number of undeniable advantages, as a result of modernization of carbamide plant got a significant reduction in operating costs:
    • Centrifugal pumps have direct drive, therefore they are compact and manufacture and installation costs as well as operating costs are significantly lower than those of piston pumps.
    • Centrifugal pumps are most suitable in cases when you want high capacity with a relatively small head, i. e. for the most chemical productions.
    • Centrifugal pumps are better suited for pumping liquids containing suspended solids, as these pumps are missing cloggy valves.
    • Due to the large gaps in the designs of centrifugal pumps compared to piston pumps, they are subject to less wear from abrasive particles present in pumped fluids. Special design of centrifugal pumps allows passage through the pump of large solid particles that is excluded in piston pumps.
    • The simplicity of the design of centrifugal pumps makes it easier to produce them from chemically resistant hard melting and hard-to-handle materials.
  • 2. Sundyne pumps are manufactured in accordance with the list of uniform standards to ensure the required production data, cost effectiveness and simplicity of details. All pumps delivered to the plant meet the uniform standards - mechanic able to exploit small pumps, can manage with the large ones.
  • 3. Full refusal from repair crew services.
  • 4. Reduction of gas contamination in the rooms. The piston machines due to their design features were permanent ammonia passes.
  • 5. Maintaining technology requirements and improving the quality of carbamide.

Today, our Uzbek specialists carry out pump maintenance and personnel training. Expansion of the Sundyne pump and spare parts park is planned.

List of pumps installed in the carbamide plant at Maxam-Chirchiq JSS
Item in flow diagram Model and year made Qty, pcs Medium RPM Operation
temperature, °C
Capacity,
m³/h
Suction
pressure, bar
Discharge
pressure, bar
1 B-601A/B,
B-602 A/B,
B-603 A/B
High-pressure
ammonia pump
LMV
341Z
6 Liquid ammonia
NH3-99,6%;
H2O-0,4%
23000 +33 40 15 200
2 D- 801 A/B,
D- 802 A/B,
D- 803 A/B
1st stage
distillation
carbonate pump
LMV
341Z
6 Ammonium
carbonate
solution
СO2-30÷36%,
NH3-40÷42%
19000 +80 7÷30 15 200
3 D–1501,
D–1502,
D–1503
2nd stage
distillation
carbonate
pump
LMV
322
3 Ammonium
carbonate
solution wth
СO2-16÷22%
NH3-30÷40%
7258 +60 4÷10 3 20
5 Е-301,
Е–302,
Е–303
Carbamide
solution
supply
pump
LMV
806
3 Carbamide solution
СO(NH2)2-70%
H2O-30%
2932 +95 45 0 5
6 H–406A,
B,C,D Pump
of urea
melt supply
to prilling tower
LMV
806
4 Urea melt
СO (NH2)2-99,7%
H2O-0,3%
2965 +135 17 0 15
7 D–901,
D–902
Secondary
steam
condensate
pump
LMV
322Z
2 Secondary
steam
condensate
pump
NH3-60g/dm³
СO(NH2)2-10g/dm³
10298 +35 2÷5 0 25
8 H-55
Pump
of waste
water supply
to hydrolysis
plant
LMV
322Z
3 Waste water
NH3-60g/dm³
СO(NH2)2-10g/dm³
10365 +80 25 3 24,96
9 900
Mechanical
seal demineralized
water supply
pump
(601, 602, 603,
801, 802, 803
– 2 stages)
P
3000
2 Demineralized
water
17663 +85 7,3+0,7 24 150
10 H-55 1/2
Pump of
waste water
supply to
hydrolysis plant
LMV
311,
2011
2 Waste water
NH3-60g/dm³
СO(NH2)2-10g/dm³
5827 +130 40 3 25
11 H–406A,
Pump of
urea melt
supply to
prilling tower
LMV
806,
2013
2 Urea melt
СO (NH2)2-99,7%
H2O-0,3%
2961 +138 17÷21 0 17.37
12 701,702
1 stage
desorption
waste water
supply pimp
LMV
806, 2012 год
2 Waste water
NH3-60g/dm³
СO(NH2)2-10g/dm³
WASTED WATER
2034 100 40 0,1 8