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CHEMICAL SCAVENGERS FOR SULPHIDES IN DRILLING FLUIDS 
– A REVIEW 
BY 
M.K. AMOSA 
I. A. MOHAMMED 
S. A. YARO 
PRESENTED AT THE 
7THCHEMCLASS CONFERENCE 2009 
THEME :– GREEN CHEMISTRY: A NEW PATHWAY IN R&D AND 
ENVIRONMENTAL CHEMISTRY 
HELD ON 11TH JUNE, 2009 AT NARICT, BASAWA, ZARIA.
Introduction 
Hydrogen Sulphide H2S 
Hydrogen Sulphide (H2S) is a colourless gas that smells like rotten eggs (from 
the sulphur). Often referred to as "sewer gas," hydrogen sulphide is highly 
poisonous as well as corrosive. Small concentrations in air may be fatal in 
minutes. Hydrogen sulphide can be found as a component of formation gases, 
dissolved in water, hydrocarbons, or even liquid sulphur (King, 1974). Thermal 
degradation of organic materials and sulphate reducing bacteria (SRB) can 
create hydrogen sulphide along with other gases. Although hydrogen sulphide 
can have adverse effects on viscosity, fluid loss, and fluid chemistry 
safety is the most important issue 
Usually, the poisoning caused by hydrogen sulphide is through inhalation and 
has a toxicity similar to cyanide. It is found in petroleum and natural gas and 
is sometimes present in ground water. (KMC Oiltools, 2006)
Introduction (Contd.) 
HYDROGEN SULPHIDE H2S 
•Relying solely on its odour is not a good idea because at 
concentrations above 100 ppm it deadens a person’s sense of smell 
within a few minutes. 
•The pure gas is heavier than air and can collect in low areas such as 
pit rooms and accommodation (KMC Oiltools, 2006). 
•The term “sulphides” used in oil and gas opeartions includes all three 
water-soluble species H2S, HS- and S2- (Garret et al, 1979).
Introduction (Contd.) 
HYDROGEN SULPHIDE H2S
CORROSION 
Introduction (Contd.) 
Dissolved H2S 
• Both the hydrogen and sulphide ions increase corrosion. 
• Hydrogen can also enter the mud by bacterial action or thermal 
degradation of organic additives. 
• Under normal conditions the hydrogen gas molecule is too large to 
enter the steel and it bubbles off . 
• In the presence of the sulphide ion, the hydrogen gradient into steel 
is increased, the hydrogen tends to attack sites that are highly 
stressed (and thus more likely to fail). 
• The hydrogen causes small cracks that lead to sudden brittle 
failure, called hydrogen embrittlement, or hydrogen stress cracking 
(Cater et al, 1985).
Introduction (Contd.) 
Dissolved H2S 
• Hydrogen generation 
depends on the pH of the 
environment . Low pH values 
increase hydrogen 
availability. 
• At pH values of less than 6, 
string failure due to H2S can 
occur in less than 1 hour. At 
pH's above 8, the time to 
failure increases to beyond 
100 hours. (KMC Oiltools, 
2006) 
11 
9 
7 
5 
3 
100 1 10 
Time to Failure (hrs.) 
pH
Introduction (Contd.) 
Dissociation of H2S with pH 
•Raising the pH is a 
good quick reaction 
to H2S … 
•However sulphide 
scavengers must be 
used as soon as 
possible because if 
the pH drops the H2S 
will form again and 
come out of solution 
(Garret et al, 1979)
Hydrogen Sulphide Scavenger Technology 
An Ideal Scavenger has to meet the following 
requirements (Garrett et al, 1979): 
 Complete, fast, and irreversible reaction with H2S under 
all mud conditions; 
 Should be able to undergo a quantitative reaction with 
sulphide; 
 pH stability of up to and beyond 11.5; 
 Non-corrosive to metals; 
 Easy and safe to handle and non-polluting to the 
environment; 
 Non detrimental to mud’s rheology; 
 Must have a good environmental acceptability before 
and after reaction with sulphide.
Environmental Concern 
Due to the high environmental awareness, there are laws 
regulating the use and discharge of chemicals after 
operations. Only the chemicals that fall within the 
GREEN/PLONOR (Posses Little Or No Risk) list could be 
discharged. 
 The offshore Oil and Gas Industry Strategy of OSPAR 
(Oslo and Paris conventions regulating offshore 
discharges) sets the objective of “… preventing and 
eliminating pollution and taking the necessary measures 
to protect the maritime area against the adverse effects 
of offshore activities so as to safeguard human health 
and of conserving marine ecosystems” OSPAR Commission. 
(OSPAR Commission, 1995) 
 “Development of new technology is important in 
reducing discharges of environmentally hazardous 
substances” Ministry of Petroleum and Energy 2005 Environmental Report. 
(OSPAR Commission, 1995)
S Scavengers A Brief Overview of the H2 used in Drilling Fluids 
Many well-known mechanisms have been employed for the 
immobilization of H2S from drilling fluid viz: 
 Copper carbonates (Carney and Jones, 1974) 
 Hydrogen peroxide (Carney and Jones, 1974) 
 Zinc compounds; especially basic zinc carbonate (Garrett et al, 
1979) 
 Iron oxide; especially magnetite (Garrett et al, 1979) 
 Chlorine containing compounds (e.g. chlorine dioxide and 
sodium hypochlorite); (Charles et al,1985) 
 Organic compounds (e.g. acrolein and formaldehyde), 
methanol, glyoxal, amines, triazines, naphthenates, chelates of 
ethylenediaminetetraacetic acid – EDTA, 
hydroxyethylethylenediaminetriacetic acid – HEDTA, 
nitrilotriacetic acid – NTA among others), etc.
 The most HSE compliant scavenger in drilling fluids so 
far is magnetite. This scavenger has a limitation of low 
reaction rates in high pH but faster rates in low pH muds 
(Garrett et al, 1979, KMC Oiltools, 2006). 
 Whereas muds’ pH are not usually allowed to go below 
9.5. It is usually between 10 and 11.5 (M-I, LLC, 2001). 
 Although commercial Zinc-containing compounds (ZCCs) 
are very effective but pose rheological and 
environmental problems (Ray et al, 1979). 
 Zinc metal has been classified as a toxic substance, 
concentrations as low as 0.15 ppm contamination could 
be potentially hazardous, hence, rendering the ZCCs as 
environmentally non-viable (Martin, 2005).
 Efficiencies of some organic compounds like Acrolein, 
Formaldehyde, and chelates like EDTA, NTA etc as 
sulphide scavengers have been reported. Their 
reactions with H2S are too complex to be predicted, 
and besides, there are outstanding questions 
concerning HSE, especially the health aspects of 
reactants and reaction products of the organic 
compounds/chelates. Formaldehyde has been 
clearly confirmed to be carcinogen (Nasr-El-Din et 
al, 2002). 
 These organic compounds and chelates usually 
renders themselves easily for sweetening purposes 
rather than application in muds (Sitz et al, 2003).
 Complexes of iron in the Fe2+ oxidation state are usually less 
sensitive to pH values (Shriver et al, 1999). 
 Fe2+, ferrous ion is a necessary trace element used by all 
known living organisms. It is also used in fertilizing aquatic 
plants (Anonymous, 2007). 
 Gluconic acid is generally recognised as safe (GRAS). Also, 
sodium, calcium and iron salts of gluconic acid have been 
confirmed mild, non-volatile, non-corrosive and non-toxic. 
They are stable up to alkaline pH values and are also stable 
at high temperatures. A metal gluconate is comparatively 
better than EDTA, NTA and other chelators (Ramachandran 
et al, 2006). 
 Most metal gluconates are confirmed HSE compliant 
materials especially the iron, sodium, zinc and calcium salts 
of gluconic acids which are used for medicinal purposes in 
both humans and animals (Ramachandran et al, 2006). 
 The inhibitive effect of calcium gluconate on carbon steel in 
neutral aqueous media has been put to test due to its non-toxic 
and eco-friendly nature and found satisfactory (Shibli 
and Kumary, 2004).
 Eric (2004) disclosed that ferrous gluconate could have an efficient 
sulphide removal from drilling fluids. 
 Amosa (2009) did more works on the use of ferrous gluconate as a 
scavenger by simulating the real well-bore operating conditions in 
the laboratory tests performed. 
 According to the OSPAR Convention GREEN/PLONOR classifications, 
this compound is found to be environmental benign and falls in 
GREEN category due to the fact that Log Pow (OECD 117) is zero 
which indicates very little potential for bioaccumulation, aerobic 
ready biodegradability in sea water using OECD 306 is very good 
(greater than 70 %) and it has a low toxicity as confirmed by the 
OSPAR protocol (OSPAR Commission, 1995). 
Probable reaction with sulphides: 
Fe (C6H12O7)2 + S2- → FeS + 2 [C6H12O7]- 
Ferrous gluconate + Sulphide →Ferrous sulphide + gluconate
Conclusions and Recommendations 
 Hydrogen sulphide scavengers are employed in more than one field applications like 
drilling operations and sweetening processes; and the type of scavenger needed for 
a particular application depends whether it can act better in that medium. 
 Although there have been many findings on sulphide scavengers, each one of them 
has one or more limitations, ranging from attributed exorbitant prices to Health, 
Safety and Environmental (HSE) problems. 
 Ferrous gluconate has been recently found to be efficient and environmentally 
benign but the laboratory tests still need be translated into real rig-site operation. It 
should also be tested in other media other than drilling fluid so as to evaluate its 
hydrogen sulphide scavenging ability in these media. 
 Optimization studies on the reaction between ferrous gluconate and hydrogen 
sulphide need be done. 
 There exist more research needs to develop or source for hydrogen sulphide 
scavengers, perhaps embodying complementary mixtures of chemicals or a 
compound specifically investigated to fit the needs and match more closely the 
qualities of an ideal scavenger. 
 Thorough testing is necessary for any particular sulphide scavenger sourced or 
designed so as to know if it has satisfactory scavenging ability in every applications; 
and if it will not adversely affect the rheology (when used in drilling mud) at various 
conditions of temperatures and pressures. Otherwise, the researcher on the 
particular scavenger should state the medium where the scavenger is mostly fit for 
application.
THANK YOU 
FOR 
LISTENING

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Review on Sulphide Scavengers for Drilling Fluids

  • 1. CHEMICAL SCAVENGERS FOR SULPHIDES IN DRILLING FLUIDS – A REVIEW BY M.K. AMOSA I. A. MOHAMMED S. A. YARO PRESENTED AT THE 7THCHEMCLASS CONFERENCE 2009 THEME :– GREEN CHEMISTRY: A NEW PATHWAY IN R&D AND ENVIRONMENTAL CHEMISTRY HELD ON 11TH JUNE, 2009 AT NARICT, BASAWA, ZARIA.
  • 2. Introduction Hydrogen Sulphide H2S Hydrogen Sulphide (H2S) is a colourless gas that smells like rotten eggs (from the sulphur). Often referred to as "sewer gas," hydrogen sulphide is highly poisonous as well as corrosive. Small concentrations in air may be fatal in minutes. Hydrogen sulphide can be found as a component of formation gases, dissolved in water, hydrocarbons, or even liquid sulphur (King, 1974). Thermal degradation of organic materials and sulphate reducing bacteria (SRB) can create hydrogen sulphide along with other gases. Although hydrogen sulphide can have adverse effects on viscosity, fluid loss, and fluid chemistry safety is the most important issue Usually, the poisoning caused by hydrogen sulphide is through inhalation and has a toxicity similar to cyanide. It is found in petroleum and natural gas and is sometimes present in ground water. (KMC Oiltools, 2006)
  • 3. Introduction (Contd.) HYDROGEN SULPHIDE H2S •Relying solely on its odour is not a good idea because at concentrations above 100 ppm it deadens a person’s sense of smell within a few minutes. •The pure gas is heavier than air and can collect in low areas such as pit rooms and accommodation (KMC Oiltools, 2006). •The term “sulphides” used in oil and gas opeartions includes all three water-soluble species H2S, HS- and S2- (Garret et al, 1979).
  • 5. CORROSION Introduction (Contd.) Dissolved H2S • Both the hydrogen and sulphide ions increase corrosion. • Hydrogen can also enter the mud by bacterial action or thermal degradation of organic additives. • Under normal conditions the hydrogen gas molecule is too large to enter the steel and it bubbles off . • In the presence of the sulphide ion, the hydrogen gradient into steel is increased, the hydrogen tends to attack sites that are highly stressed (and thus more likely to fail). • The hydrogen causes small cracks that lead to sudden brittle failure, called hydrogen embrittlement, or hydrogen stress cracking (Cater et al, 1985).
  • 6. Introduction (Contd.) Dissolved H2S • Hydrogen generation depends on the pH of the environment . Low pH values increase hydrogen availability. • At pH values of less than 6, string failure due to H2S can occur in less than 1 hour. At pH's above 8, the time to failure increases to beyond 100 hours. (KMC Oiltools, 2006) 11 9 7 5 3 100 1 10 Time to Failure (hrs.) pH
  • 7. Introduction (Contd.) Dissociation of H2S with pH •Raising the pH is a good quick reaction to H2S … •However sulphide scavengers must be used as soon as possible because if the pH drops the H2S will form again and come out of solution (Garret et al, 1979)
  • 8. Hydrogen Sulphide Scavenger Technology An Ideal Scavenger has to meet the following requirements (Garrett et al, 1979):  Complete, fast, and irreversible reaction with H2S under all mud conditions;  Should be able to undergo a quantitative reaction with sulphide;  pH stability of up to and beyond 11.5;  Non-corrosive to metals;  Easy and safe to handle and non-polluting to the environment;  Non detrimental to mud’s rheology;  Must have a good environmental acceptability before and after reaction with sulphide.
  • 9. Environmental Concern Due to the high environmental awareness, there are laws regulating the use and discharge of chemicals after operations. Only the chemicals that fall within the GREEN/PLONOR (Posses Little Or No Risk) list could be discharged.  The offshore Oil and Gas Industry Strategy of OSPAR (Oslo and Paris conventions regulating offshore discharges) sets the objective of “… preventing and eliminating pollution and taking the necessary measures to protect the maritime area against the adverse effects of offshore activities so as to safeguard human health and of conserving marine ecosystems” OSPAR Commission. (OSPAR Commission, 1995)  “Development of new technology is important in reducing discharges of environmentally hazardous substances” Ministry of Petroleum and Energy 2005 Environmental Report. (OSPAR Commission, 1995)
  • 10. S Scavengers A Brief Overview of the H2 used in Drilling Fluids Many well-known mechanisms have been employed for the immobilization of H2S from drilling fluid viz:  Copper carbonates (Carney and Jones, 1974)  Hydrogen peroxide (Carney and Jones, 1974)  Zinc compounds; especially basic zinc carbonate (Garrett et al, 1979)  Iron oxide; especially magnetite (Garrett et al, 1979)  Chlorine containing compounds (e.g. chlorine dioxide and sodium hypochlorite); (Charles et al,1985)  Organic compounds (e.g. acrolein and formaldehyde), methanol, glyoxal, amines, triazines, naphthenates, chelates of ethylenediaminetetraacetic acid – EDTA, hydroxyethylethylenediaminetriacetic acid – HEDTA, nitrilotriacetic acid – NTA among others), etc.
  • 11.  The most HSE compliant scavenger in drilling fluids so far is magnetite. This scavenger has a limitation of low reaction rates in high pH but faster rates in low pH muds (Garrett et al, 1979, KMC Oiltools, 2006).  Whereas muds’ pH are not usually allowed to go below 9.5. It is usually between 10 and 11.5 (M-I, LLC, 2001).  Although commercial Zinc-containing compounds (ZCCs) are very effective but pose rheological and environmental problems (Ray et al, 1979).  Zinc metal has been classified as a toxic substance, concentrations as low as 0.15 ppm contamination could be potentially hazardous, hence, rendering the ZCCs as environmentally non-viable (Martin, 2005).
  • 12.  Efficiencies of some organic compounds like Acrolein, Formaldehyde, and chelates like EDTA, NTA etc as sulphide scavengers have been reported. Their reactions with H2S are too complex to be predicted, and besides, there are outstanding questions concerning HSE, especially the health aspects of reactants and reaction products of the organic compounds/chelates. Formaldehyde has been clearly confirmed to be carcinogen (Nasr-El-Din et al, 2002).  These organic compounds and chelates usually renders themselves easily for sweetening purposes rather than application in muds (Sitz et al, 2003).
  • 13.  Complexes of iron in the Fe2+ oxidation state are usually less sensitive to pH values (Shriver et al, 1999).  Fe2+, ferrous ion is a necessary trace element used by all known living organisms. It is also used in fertilizing aquatic plants (Anonymous, 2007).  Gluconic acid is generally recognised as safe (GRAS). Also, sodium, calcium and iron salts of gluconic acid have been confirmed mild, non-volatile, non-corrosive and non-toxic. They are stable up to alkaline pH values and are also stable at high temperatures. A metal gluconate is comparatively better than EDTA, NTA and other chelators (Ramachandran et al, 2006).  Most metal gluconates are confirmed HSE compliant materials especially the iron, sodium, zinc and calcium salts of gluconic acids which are used for medicinal purposes in both humans and animals (Ramachandran et al, 2006).  The inhibitive effect of calcium gluconate on carbon steel in neutral aqueous media has been put to test due to its non-toxic and eco-friendly nature and found satisfactory (Shibli and Kumary, 2004).
  • 14.  Eric (2004) disclosed that ferrous gluconate could have an efficient sulphide removal from drilling fluids.  Amosa (2009) did more works on the use of ferrous gluconate as a scavenger by simulating the real well-bore operating conditions in the laboratory tests performed.  According to the OSPAR Convention GREEN/PLONOR classifications, this compound is found to be environmental benign and falls in GREEN category due to the fact that Log Pow (OECD 117) is zero which indicates very little potential for bioaccumulation, aerobic ready biodegradability in sea water using OECD 306 is very good (greater than 70 %) and it has a low toxicity as confirmed by the OSPAR protocol (OSPAR Commission, 1995). Probable reaction with sulphides: Fe (C6H12O7)2 + S2- → FeS + 2 [C6H12O7]- Ferrous gluconate + Sulphide →Ferrous sulphide + gluconate
  • 15. Conclusions and Recommendations  Hydrogen sulphide scavengers are employed in more than one field applications like drilling operations and sweetening processes; and the type of scavenger needed for a particular application depends whether it can act better in that medium.  Although there have been many findings on sulphide scavengers, each one of them has one or more limitations, ranging from attributed exorbitant prices to Health, Safety and Environmental (HSE) problems.  Ferrous gluconate has been recently found to be efficient and environmentally benign but the laboratory tests still need be translated into real rig-site operation. It should also be tested in other media other than drilling fluid so as to evaluate its hydrogen sulphide scavenging ability in these media.  Optimization studies on the reaction between ferrous gluconate and hydrogen sulphide need be done.  There exist more research needs to develop or source for hydrogen sulphide scavengers, perhaps embodying complementary mixtures of chemicals or a compound specifically investigated to fit the needs and match more closely the qualities of an ideal scavenger.  Thorough testing is necessary for any particular sulphide scavenger sourced or designed so as to know if it has satisfactory scavenging ability in every applications; and if it will not adversely affect the rheology (when used in drilling mud) at various conditions of temperatures and pressures. Otherwise, the researcher on the particular scavenger should state the medium where the scavenger is mostly fit for application.
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