- Greatly improved performance and durability over conventional pressure reducing valves.
- Spherical master valve provides good sealing and reduced seat leakage (ANSI Class IV).
- Meets Japan Society of Heating, Air Conditioning and Sanitary Engineers' Society of Heating, Air Conditioning and Sanitary Engineers SHASE-S106 standard for pressure reducing valves.
- Simple and reliable design of internal parts.
| Model | GP-1000-1001 | GP-1002 | GP-1010 | GP-1200 | GP-1210 | GP-1000EN | ||
| Application | Steam | |||||||
| Inlet pressure | 0.1-1.0 MPa | 0.1-0.5 MPa | 0.1-1.0 MPa | |||||
| Under pressure | 0.05-0.9 MPa | 0.03-0.15 MPa | 0.05-0.9 MPa | |||||
| Up to 90% of inlet pressure (gauge) | ||||||||
| Min. differential pressure | 0.05 MPa | |||||||
| Max. coeff. pressure reduction | 20: 1 | |||||||
| Maximum temperature | 220 ° C | |||||||
| Valve seat leaks | No more than 0.01% of nominal flow | |||||||
| Material | Corpus | Ductile Iron | ||||||
| Valve, valve seat | Stainless steel | |||||||
| Plunger, cylinder | Bronze or brass | |||||||
| Connection | JIS 10K FF with flange. connection | JIS Rc threaded. connection | JIS 10K FF with flange connection | JIS Rc Threaded connection | EN PN16 with flange connection | |||
- Available with stainless steel plug and cylinder parts.
Description of GP-1000 Series model code



Nominal Sizes Selection Chart (For Steam)

Example 1
When selecting the nominal size of a pressure reducing valve whose inlet pressure (P1), reduced pressure (P2), and steam flow rate are 0.6 MPa, 0.4 MPa, and 800 kg/h, respectively, first find intersection point (A) of the inlet pressure of 0.6 MPa and the reduced pressure of 0.4 MPa. Trace down vertically from this intersection point to find intersection point (B) with the flow rate of 800 kg/h. Since intersection point (B) lies between nominal sizes 40A and 50A, select the larger one, 50A.
Example 2
When selecting the nominal size of a pressure reducing valve whose inlet pressure (P1), reduced pressure (P2), and steam flow rate are 0.8 MPa, 0.05 MPa, and 600 kg/h, respectively, first find intersection point (C) of the inlet pressure of 0.8 MPa and the diagonal line. Trace down to the left from this intersection point to find intersection point (D) with the reduced pressure of 0.05 MPa. Trace down vertically from intersection point (D) to find intersection point (E) with the flow rate of 600 kg/h. Since intersection point (E) lies between nominal sizes 32A and 40A, select the larger one, 40A. ∙ Set the safety factor at 80 to 90%.
Specifications Selection Chart

Find the intersection point of the inlet and reduced pressures. If the intersection point is within any of the ranges shown in the chart above, the pressures are controllable. ∙ Range (A) and (C): GP-1000 Series except GP-1002 and 1012 ∙ Range (B) and (C): GP-1002 and 1012
Corrected Cv value

Example Take a pressure reducing valve whose inlet pressure is 0.8 MPa, the reduced pressure is 0.05 MPa. Find the inlet and reduced pressure intersection point (A) at the above chart, then draw a horizontal line in the leftward direction to pint (B) which indicates a correction coefficient of 0.85. For a nominal size of 25A, the corrected Cv value would be calculated as follows: 4 (rated Cv value) 0.85 (correction coefficient) = 3.4
Flow Characteristic Chart

Pressure Characteristic Chart

This chart shows variation in reduced pressure when the inlet pressure of 1.0 MPa is changed between 0.3 MPa and 1.0 MPa while the reduced pressure is set at 0.1 MPa.
Delivery
- Delivery by Poland with DHL courier service to the branch - free
- Delivery by Poland with DHL courier service to the branch at the address ("from door to door") - free
Payment
- Cashless payment with VAT: OPEKS Energysystems sp.z.o.o., TIN 5273030184, Santander Bank Polska S.A., SWIFT: WBKPPLPP, account number: 69 1090 1056 0000 0001 5227 8036, IBAN: PL69 1090 1056 0000 0001 5227 80
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