U.S. patent number 3,885,914 [Application Number 05/367,083] was granted by the patent office on 1975-05-27 for polymer-zinc corrosion inhibiting method.
This patent grant is currently assigned to Calgon Corporation. Invention is credited to William Robert Hollingshad, Paul Hotchkiss Ralston.
United States Patent |
3,885,914 |
Hollingshad , et
al. |
May 27, 1975 |
Polymer-zinc corrosion inhibiting method
Abstract
Use of low molecular weight polymers and zinc to inhibit the
corrosion of metals by oxygen-bearing waters.
Inventors: |
Hollingshad; William Robert
(Bethel Park, PA), Ralston; Paul Hotchkiss (Pittsburgh,
PA) |
Assignee: |
Calgon Corporation (Pittsburgh,
PA)
|
Family
ID: |
23445866 |
Appl.
No.: |
05/367,083 |
Filed: |
June 4, 1973 |
Current U.S.
Class: |
422/16;
252/389.52; 252/396; 422/19; 252/392; 422/17 |
Current CPC
Class: |
C23F
11/08 (20130101) |
Current International
Class: |
C23F
11/08 (20060101); C23f 007/10 () |
Field of
Search: |
;21/2.7R
;252/180,390,401 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Padgett; Benjamin R.
Assistant Examiner: Walsh; Donald P.
Attorney, Agent or Firm: Westlake; Harry E. Anderson;
Rudolph J. Katz; Martin L.
Claims
We claim:
1. A method of inhibiting the corrosion of metals in a water system
comprising maintaining in the water of said system at least about 5
ppm of a composition comprising zinc and at least one low molecular
weight polymer selected from the group consisting of
polyacrylamide, poly acrylic acid and sodium polacrylate.
2. A method as in claim 1 wherein the polymer has a molecular
weight of from about 500 to about 10,000.
3. A method as in claim 1 wherein the ratio of polymer to zinc is
from about 1:3 to about 5:1 by weight.
4. A method as in claim 1 wherein the ratio of polymer to zinc is
from about 3:1 to about 4:1.
Description
BACKGROUND OF THE INVENTION
This invention relates to the inhibition of corrosion in water
systems which utilize oxygen-bearing waters.
More particularly, this invention relates to the use of
compositions comprising low molecular weight polymers and zinc to
inhibit the corrosion of metals in water systems which contain
oxygen-bearing waters.
Oxygen corrosion is, of course, a serious problem in any
metal-containing water system. The corrosion of iron and steel is
of principal concern because of their extensive use in many types
of water systems. Copper and its alloys, aluminum and its alloys,
and galvanized steel are also used in water systems and are subject
to corrosion. We have discovered novel corrosion inhibitors which
will inhibit oxygen corrosion in water systems containing such
metals.
SUMMARY OF THE INVENTION
We have found that compositions comprising low molecular weight
polymers and zinc are effective corrosion inhibitors. Suitable
polymers include water-soluble salts of acrylic acid, acrylates,
methacrylates, unhydrolyzed or partially hydrolyzed acrylamides,
and acrylamidomethyl propane sulfonates. The polymers may be homo-,
co-, or ter- polymers of any of the aforementioned polymers and may
have a molecular weight of from about 500 to about 10,000. The
preferred molecular weight, however, is about 1,000. Suitable
water-soluble salts include the alkali metal, alkaline earth metal,
zinc, cobalt, ammonium or amino and lower alkanol amine salts.
The zinc ion may be supplied in many ways. For example, the zinc
ion may be added by utilizing a water-soluble zinc salt, such as,
zinc chloride, zinc acetate, zinc nitrate, and zinc sulfate, which
forms zinc ions in aqueous solution. The zinc ion may also be
supplied by adding zinc just to a solution of the polymer.
Our corrosion-inhibiting compositions can contain a ratio of
polymer to zinc of from about 1:3 to about 5:1 by weight. The
preferred ratio, however, is from about 3:1 to 4:1 by weight. These
compositions will effectively inhibit corrosion of metals when
maintained in a water system at a concentration of at least about 1
ppm at the above ratios and, preferably, about 5 to 50 ppm. Maximum
concentrations are determined by the economic considerations of the
particular application.
Compounds such as benzotriazole or mercaptobenzothiazole may be
added to the final formulation in varying amounts to improve its
usefulness in a wider variety of industrial applications where both
steel and copper or its alloys are present in the same system.
The following table illustrates the effectiveness of polyacrylic
acid (molecular weight about 1,000) and a partially hydrolyzed
polyacrylamide (molecular weight about 7,000) when used with and
without zinc at the dosages and pH indicated.
The test procedure used was a standard 5-day continuous immersion,
mild agitation test carried out in synthetic Pittsburgh tap water
for 5 days (95.degree.F.). Steel corrosion rates are noted in the
following table:
TABLE 1 ______________________________________ Weight/Loss
Corrosion Rate Data for Polymers of Polyacrylic Acid and Partially
Hydrolyzed Polyacrylamide With and Without Zinc Inhibitor Partially
Hydrolyzed Polyacrylic Polyacrylamide Corrosion Acid (ppm)
Zn.sup.+.sup.+ Rate (mdd) pH ______________________________________
0 0 0 200 7.2-7.4 0 10 0 143 6.6-7.0 0 10 10 14 6.2-7.0 30 0 0 152
6.1-6.1 30 0 10 23 -- ______________________________________
The following table illustrates the influence of the ratio of
polymer to zinc on several corrosion-inhibiting compositions of
this invention. These tests were run in synthetic Pittsburgh water.
Steel electrodes were used in polarization test cells with the
initial pH at 7.0. Inhibitor concentrations were calculated on the
basis of active material. The amount of corrosion that had taken
place was determined from the current density at the intersection
of an extrapolation of the so-called "Tafel" portion of the anodic
polarization curve with the equilibrium or "mixed" potential value,
usually referred to as the corrosion potential, "E.sub.corr ".
Application of Faraday's Law allows a computation of a direct
mathematical relationship between the current density at
E.sub.corr, expressed in amperes per square centimeter and a more
useful corrosion rate expression such as milligrams of steel
consumed per square decimeter of surface per day (m.d.d.) and mils
per year (m.p.y.). This relationship is such that a current density
value of 4.0.times.10.sup..sup.-7 amperes/cm.sup.2 .times.1.0
mg/dm.sup.2 /day. Further, the m.p.y. value is calculated from the
usual formula: m.p.y..times.m.d.d..times.1.44/density, using a
density value of 7.87 g/cm.sup.3 for steel. The corrosion rate for
steel in this water without inhibitor is 100 mdd. This control
value applies to both Tables 2 to 3.
TABLE 2
__________________________________________________________________________
Polarization Corrosion Rate Data to Illustrate the Influence of
Various Polymer to Zinc Weight Ratios (mdd) Weight Ratio Polymer to
Zinc .fwdarw. 1 : 2 1 : 1 2 : 1 3 : 1 4 : 1 5 :
__________________________________________________________________________
1 Polymer Dosage (mg/l) .fwdarw. 10 30 100 10 30 100 10 30 100 10
30 100 10 30 10 30
__________________________________________________________________________
Polymer Used Polyacrylic Acid 36 3 3 35 62 4 80 54 17 42 38 3 17 6
30 7 Sodium Polyacrylate 69 52 25 46 48 34 1 31 1 2 8 1 4 1 58 6
Partially Hydrolyzed Polyacrylamide 80 -- -- 43 -- -- 32 3 -- 67 3
-- 51 66 80 66
__________________________________________________________________________
The following table illustrates that the effectiveness of polymeric
corrosion inhibitors decreases as the molecular weight
increases.
TABLE 3 ______________________________________ Polarization
Corrosion Rate Data for Sodium Polyacrylates Approximate Dosages
(mg/l) Corrosion Rate Molecular Weight Polymer Zinc (mdd)
______________________________________ 900 30 10 8 900 100 33 1
2,500 30 0 73 2,500 30 10 70 2,500 100 30 50 5,000 30 0 74 5,000 30
10 48 5,000 100 30 61 10,000 30 0 67 10,000 30 10 76 10,000 100 0
53 10,000 100 30 56 ______________________________________
* * * * *