worthington mud pump free sample

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We service a long list of Worthington pumps, including the MF, MN and MC series. If the make or model you are looking for does not appear on our Worthington list, please contact us, as updates may be available.

For replacement parts for your municipal water, wastewater or sewage pump systems, including parts for Allis Chalmers, Aurora, Crane Deming, Fairbanks Morse, Paco and Worthington pumps, call Abba Pump Parts & Service at 1-800-268-5142 today!

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I’ve run into several instances of insufficient suction stabilization on rigs where a “standpipe” is installed off the suction manifold. The thought behind this design was to create a gas-over-fluid column for the reciprocating pump and eliminate cavitation.

When the standpipe is installed on the suction manifold’s deadhead side, there’s little opportunity to get fluid into all the cylinders to prevent cavitation. Also, the reciprocating pump and charge pump are not isolated.

The suction stabilizer’s compressible feature is designed to absorb the negative energies and promote smooth fluid flow. As a result, pump isolation is achieved between the charge pump and the reciprocating pump.

The isolation eliminates pump chatter, and because the reciprocating pump’s negative energies never reach the charge pump, the pump’s expendable life is extended.

Investing in suction stabilizers will ensure your pumps operate consistently and efficiently. They can also prevent most challenges related to pressure surges or pulsations in the most difficult piping environments.

We have a large stock of Double-Acting Duplex Pumps that are used for various applications such as fluid (including heavy oil) transfers in pipelines, mud pumping, cement pumping, water well drilling etc. in the Oil & Gas, Agriculture, Mining, Municipal & Manufacturing sectors. Duplex Pumps have two cylinders and are capable of handling different pressures, volumes and flow rates. We supply new, used and refurbished API 674 Double Acting Duplex Pumps of all leading manufacturers including Gaso, Wheatley, Gardner Denver, National & Oilwell.

In a patent assigned to the assignee of the present application (Nuclear Magnetic Logging Method, A. E. Worthington, issued June 8, 1965, now Patent No. 3,188,- 55 6), there is disclosed a method of reducing the relaxation times of protons of water within an earth formation relative to the relaxation times of protons of crude oil within such formation to aid in determining the presence of such oil. In the method, a molecular paramagnetic material such as molecular oxygen is added to the drilling fluid circulating through the well bore. The molecular oxygen, being soluble in water, penetrates the filter cake formed at the side wall of the well bore, and diffuses throughout the formation water to reduce the nuclear magnetism relaxation times of the protons of such water. Not all the molecular oxygen passes into the earth formation, however. The portion of the oxygen not passing into the earth formation is an oxidizing agent and creates an extremely corrosive environment in the well bore. Such an environment is undesirable when the well bore is later cased with metallic pipe. Attempts have been made to remedy the corrosion problems caused by oxygen remaining in the well bore. Another method of reducing the relaxation times of water protons attempts to utilize soluble ionized paramagnetic metal salts in drilling fluids in a manner similar to the molecular oxygen. However, it has been found that such metal salts have a tendency to be incompatible with weakly-basic drilling fluids forming insoluble hydroxide compounds that increase the viscosity of the treated fluid and the volume of filtrate passing into the formation. Since most drilling fluids commercially available are weakly-basic, it would be desirable to be able to admix ionized paramagnetic metal salts with weakly-basic drilling fluids without disturbing rheological and filtration properties of such treated fluids. (In this application, the term weakly basic drilling fluid signifies a fluid having an upper pH limit of 12.4 and a preferred range of from about 8l2.)

Admixing the formed manganese chelate dispersion or solution with the untreated drilling fluid, preferably but not necessarily, is achieved by means of a T coupling section connected to the mud pumps, the mix tankfand the drilling fluid reservoir, respectively. In operation, drilling fluid enters through a first port of the T section, admixes with the chelate compound entering through a second port, and exits (along With the chelate compound) through a third port connected to the Well bore. The volume of chelate solution to be absorbed by the drilling fluid varies in accordance with the above-listed ranges of constituency. Hence, adjustment (by valves at the T section) of the flow rates of the manganese chelate solution and the untreated drilling fluid may be necessary to assure adequate amounts of manganese chelate compound in the treated drilling fluid.

Characteristics of several muds containing the addition of 1.1 p.p.b. of manganese metal EDTA chelate compound prepared in the above manner is shown in Table I. The samples were tested in accordance with API Bulletin RP13B (Standard Procedure for Testing Drilling Fluids, November 1962), Section 2 (paragraphs 2.7 to 2.11), and Section 6.

Viscosity (cp.) 1. 26 17 Yield Point (lbs/100 it?) 33 23 10 min. gel strength (lb./100 itfi)- 97 81 pH 8.2 9. 1 Temperature, F 70 70 2 Gypsum-Q-Broxin Mud with Emulsified Oil:

Viscosity (cp.) 17 Yield Point (lbs/100 it?) 13 9 10 min. gel strength (lb./100 it?) 18 14 pH 8.5 8.7 Temperature, F 70 70 3 Low pH Diesel Oil Emulsion Mud:

Viscosity (cp.) 17 16 Yield Point (lbs/100 ft?) 8 9 10 min. gel strength (UL/100 ftfl)- 3 6 p 7. 9 8. 5 Temperature, F 70 70 4 High pH, Lime-Lignite Emulsion Mud:

Characteristics of several muds containing the addition of 1.1 p.p.b. of iron EDTA compound prepared in the above manner are shown in Table II. The samples were tested in accordance with API Bulletin RP13B (Standard Procedure for Testing Drilling Fluids, November 1962), Section 2 (paragraphs 2.7 to 2.11), and Sec- 1 tion 6.

Viscosity (01).) -1 26 18 Yield Point (lbs/ it?) 33 19 10 min. gel strength (lb/100 tt. 97 87 pH 8. 2 8. 8 Temperature, F 70 70 2 Gypsum-Q-Broxin Mud sified Oil:

Viscosity (cp.) 15 16 Yield Point (lbs/100 ft?) 13 11 10 min. gel strength (lb/100 it?) 18 10 pH 8. 5 8. 3 Temperature, F. 70 70 3 Low pH Diesel Oil Emul on Viscosity (c 17 14 Yield Point (lbs/100 it?) 8 7 10 min. gel strength (lb. [100 it!) 3 6 pH 7. 9 7. 9 Temperature,F 11 70 70 4 High pH, Lime-Lignite Emulsion Mud:

The data of Table III indicate that manganese EDTA chelate compounds formed in the above manner and added to drilling fluids are superior to iron chelate compounds in that the former have greater effect in lowering the relaxation time of the filtrates of these fluids. It is noted that an exception exists for improvement of the diagnostic ability of a nuclear well log where the drilling fluid is a high pH (12.4) lime-lignite emulsion mud (Sample 4). That sample shows little or no improvement in relaxation time inhibitors for either the manganese or iron chelate compound.