EP0099884A1 - Procede et dispositif de traitement de debris rocheux de forages - Google Patents

Procede et dispositif de traitement de debris rocheux de forages

Info

Publication number
EP0099884A1
EP0099884A1 EP82900860A EP82900860A EP0099884A1 EP 0099884 A1 EP0099884 A1 EP 0099884A1 EP 82900860 A EP82900860 A EP 82900860A EP 82900860 A EP82900860 A EP 82900860A EP 0099884 A1 EP0099884 A1 EP 0099884A1
Authority
EP
European Patent Office
Prior art keywords
tube
stage
hydrocarbons
cuttings
slurry
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP82900860A
Other languages
German (de)
English (en)
Other versions
EP0099884A4 (fr
Inventor
Herman J. Schellstede
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Publication of EP0099884A1 publication Critical patent/EP0099884A1/fr
Publication of EP0099884A4 publication Critical patent/EP0099884A4/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • E—FIXED CONSTRUCTIONS
    • E21—EARTH OR ROCK DRILLING; MINING
    • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B41/00—Equipment or details not covered by groups E21B15/00 - E21B40/00
    • E21B41/005—Waste disposal systems
    • E—FIXED CONSTRUCTIONS
    • E21—EARTH OR ROCK DRILLING; MINING
    • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B21/00—Methods or apparatus for flushing boreholes, e.g. by use of exhaust air from motor
    • E21B21/06—Arrangements for treating drilling fluids outside the borehole
    • E21B21/063—Arrangements for treating drilling fluids outside the borehole by separating components
    • E21B21/065—Separating solids from drilling fluids
    • E21B21/066—Separating solids from drilling fluids with further treatment of the solids, e.g. for disposal
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
    • F26B17/18—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by rotating helical blades or other rotary conveyors which may be heated moving materials in stationary chambers, e.g. troughs
    • F26B17/22—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by rotating helical blades or other rotary conveyors which may be heated moving materials in stationary chambers, e.g. troughs the axis of rotation being vertical or steeply inclined
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B23/00—Heating arrangements
    • F26B23/02—Heating arrangements using combustion heating
    • F26B23/022—Heating arrangements using combustion heating incinerating volatiles in the dryer exhaust gases, the produced hot gases being wholly, partly or not recycled into the drying enclosure
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00—Drying solid materials or objects by processes involving the application of heat
    • F26B3/18—Drying solid materials or objects by processes involving the application of heat by conduction, i.e. the heat is conveyed from the heat source, e.g. gas flame, to the materials or objects to be dried by direct contact
    • F26B3/22—Drying solid materials or objects by processes involving the application of heat by conduction, i.e. the heat is conveyed from the heat source, e.g. gas flame, to the materials or objects to be dried by direct contact the heat source and the materials or objects to be dried being in relative motion, e.g. of vibration

Definitions

  • the invention relates to oil field technology, particularly in the drilling of production oil well apparatus. Although not limited to any particular location of use, the invention has particular utility at locations of drilling along the continental shelf, where environmental problems are particularly acute when oil base drilling muds are employed.
  • the invention provides an apparatus and method for removing hydrocarbons adhering to fragments of rock produced in drilling of wells, particularly where an oil base drilling fluid is used.
  • a primary object of the invention is to remove the film or layer of oily components of oil base drilling fluid from cuttings formed in oil and gas well drilling operations.
  • Another object is to provide a method and apparatus for effectively using gaseous products formed by volatilizing hydrocarbons adhering to drill cuttings. Still another object is to provide a cuttings burner apparatus having a heating zone for final removal of hydrocarbons characterized by a high degree of resistance to corrosion, erosion, and chemical attack from volatile products formed therein. Yet another object is to form a continuous two-stage apparatus and process for burning hydrocarbons and other volatile materials from cuttings, where each stage is carried out in an apparatus having a common shaft for transfer of materials into the first stage, from the first to the second stage, and from the second stage in oil-free form from the apparatus.
  • Yet another object is to provide apparatus which generates a portion of the heat required for operation of the burner from waste gaseous products resulting from the heating of the cuttings.
  • a further object is to provide recovery of waste heat by injection of oxygen into the stream of evolved hydrocarbon vapors.
  • Still a further object is to provide a method for accomplishing the preceding objects.
  • Another further object is to provide a processed pulverized solid product which contains less than one part per million of hydrocarbons.
  • Figure 1 is a sectional view of a preferred form pf the invention in which two stages of treatment are provided with the stages being connected by a common shaft for operation of each stage and for transfer of materials to and from each stage.
  • Figure 2 is a side elevational view of a second form of the invention, partly broken away to show internal components, where the first stage has a conical surface on the interior of which incoming contaminated cuttings are applied and from which heated cuttings are removed by flaking, scraping or the like; the first stage and second stage of the second form of the invention are connected by a common shaft for transfer of materials through the second stage and between stages.
  • Figure 3 is a transverse sectional view of the apparatus of Fig. 1, taken substantially upon a plane passing along section line 3—3 on Fig. 1.
  • Figure 4 is a transverse sectional view of the apparatus of Fig. 1, taken substantially upon a plane passing along section line 4—4 of Fig. 1.
  • Figure 5 is a transverse sectional view of the apparatus of Fig. 1, taken substantially upon a plane passing along section line 5—5 of Fig. 1.
  • Figure 6 is an enlarged fragmentary sectional view, similar to a portion of Fig. 3, showing the laminar flow with a liquified inner and outer layers. DESCRIPTION OF THE PREFERRED EMBODIMENTS
  • Drilling fluid is continuously pumped into the drill hole and the cuttings or material cut from the formation are suspended in the fluid and raised to the surface for separation and recycling of the drilling fluid back into the drill hole. While water base drilling fluids are suitable for drilling in certain geological formations, in certain other formations it is necessary or desirable to use an oil base drilling fluid.
  • Cuttings burner apparatus 10 is comprised of first stage 12, second stage 14, and gas collection and recycling leg 16. Combined drilling fluid and drill cuttings are pumped to a storage receptacle until ready for processing. The contaminated cuttings are mechanically separated from recyclable drilling fluid at a gravity screen or shale shaker and are then introduced into a surge hopper to allow for variation is feed rates.
  • First stage 12 accordingly comprises inlet pipe 20 for receiving contaminated cuttings in the form of slurry from the surge hopper, the slurry entering plenum 22, where auger 24 forces the slurry in plenum 22 downwardly into and through the first stage 12.
  • Auger 24 has blades mounted on shaft 26, which is powered by drive means (not shown) for rotation in a clockwise direction, viewed from above.
  • Shaft 26 coincides with the axis of the apparatus 10 and enables all materials transfer operations to be conducted from a single source of drive means.
  • First stage drum 30 rotates with shaft 32, concentric with shaft 26 and powered by the same drive means, and drum 30 is provided with two flights 34 of blades to urge material undergoing treatment in first stage 12 downwardly through tube 36.
  • Drum 30 is rotatable, and tube 36 can also be rotated to vary the relative speed of rotation between drum 30 and tube 36. Accordingly, tube 36 is mounted on bearing 38, and can be driven by worm gear 40 at a desired speed of rotation in either the clockwise or counterclockwise direction.
  • Tube 36 is preferably constructed of a corrosion resistant high-temperature alloy, such as a chromium-nickel alloy sold under the trademark, "Inconel”. Heating coils 42 or other heating devices surround or are associated with the heated portion of tube 36 to raise the temperature of the tube and cuttings forced through the gap 44 between drum 30 and tube 36 to a temperature of about 1400°F. (760°C).
  • first stage 12 Evolution of the major portion of the hydrocarbon materials occurs in first stage 12, such gases passing upwardly into receiving chamber 46 and thence downwardly through annular space 48 in the direction of the arrows.
  • Shaft 32 is centered within housing 50 with the aid of air cooled bearings 52.
  • Insulation material 54 aids in retaining heat otherwise lost by radiation, conduction, or convection.
  • Result of heating in first stage 12 is to dry the incoming cuttings somewhat and to form a cake within gap 44 as volatilized gases begin to be evolved.
  • the cake which is still a slurry is continuously removed under the influence of blades 34, falls into discharge region 60 where further evolution of gases can occur, all gases emerging from discharge region 60 into gas recycle pipe 62.
  • Cuttings fall into the second stage 14 from reducing tube section 66 and pass into through heat gap 68 of second stage 14.
  • Gap 68 is formed between second stage drum 70 and second stage tube 72, which is also preferably constructed of a nickel-chromium alloy capable of withstanding the high temperatures, typically about 2600°F.
  • die block 80 allows any unburned gases, entrained in the cuttings, to be vented through a collecting manifold 82 and recycled through gas collection and recycling leg 16.
  • the now acceptable effluent exits the device through exit tube 84 where a water spray formed from water inlet 86 can serve to cool and consolidate the material for pelletizing or otherwise placing into a convenient form for handling or form a slurry which may be discharged at the ocean floor.
  • the emergent material can be disposed of without concern for potential jeopardy due to violation of ecological or environmental regulations.
  • tube 72 is heated electrically by resistance heating between electrodes 88 and 90, although other means of heating can also be used, such as induction heating, provision of coils similar to those of coils 42, and the like.
  • Drum 70 is heated internally through combustion of volatilized gases entering through recycle tube 94 of leg 16. Pressureized air or oxygen enters through line 96 and complete combustion occurs within drum 70, the exhaust gases exiting through perforations 98 on shaft 100. Maintenance of a desired pressure in drum 70 is possible with use of gas lock arrangement 102. Additional air or oxygen input through line 104 furnishes heating for lower arm 106, which is used for heating of die block 80, with combustion gases exiting through exhaust 108 to a flare burn off or the like. The arrangement of the lower portion of the apparatus is best seen in Fig. 5, where the swirling action obtainable is readily visible.
  • Channels 110 in die block 80 direct the product through orifices 112 where pulverization occurs and where selection of the orifice size and number determines the pressure obtainable in second stage 14.
  • Drum 70 is held on shaft 114 and rotates as shaft 114 rotates in a clockwise direction. Igniter 116 insures complete combustion of gases in the lower part of gas collection and recycling leg 16. In order to minimize heat losses, insulation can be placed in region 120 between tube 72 and housing 122.
  • tube 72 and drum 70 are made of a nickel-chronium alloy sold under the name "Inconel" .
  • apparatus 10 Due to the closed loop venting of combustible gases within the system, apparatus 10 poses little hazard at drilling sites and its straight line design and single drive shaft allow it to be rigged between decks or outboard of the platform of an offshore drilling rig, thereby minimizing the space requirements for installation.
  • the electrical requirements can be easily handled without burdening generators furnishing power for other purposes.
  • the unit is self-contained and therefore easily portable. After the operating temperature has been reached the combustible products will substantially maintain operating temperatures in most instances whereby the electrical power requirements for heating are dramatically reduced, and through-heating can produce operational efficiencies as high as 90%.
  • the preferred temperature of 2600°F. (1425.2°C.) in the second stage 16 is easily obtainable.
  • cuttings separated from recyclible oil base drilling fluid at a share are automatically introduced from a surge hopper into inlet pipe 130 of the device of Fig. 2 shown generally by the numeral 132.
  • the raw cuttings from pipe 130 enter first stage 134 and are then transferred to second stage 136, with recycling of evolved gases in a closed recycling loop 138.
  • Drive means 140 rotate shaft 142 which drives first stage 134 on shaft 144, and drives screw conveyor 146 on shaft 148, as well as driving dust slinger 150 through shaft 152.
  • Drive means 140 is an electric drive motor operating at low speed and high torque, having a selectable low speed drive shaft 142 or a high speed drive shaft 142 and appropriate gearing within gear box 153.
  • Raw cuttings from inlet pipe 130 pass into first stage 134 by slinger ring 158, which deposits the raw contaminated cuttings evenly on the interior surface 160 of cone 164.
  • induction type heater coils 162 cone 164 causes preheating of the cuttings to approximately 1400°F. (760°C).
  • the cuttings are dried somewhat and form a cake on the interior surface 160 of cone 164 and begin to give up volatilized gases which are gathered into pipe 170 by blower 172.
  • the cake formed on the interior of cone is continuously removed by scraper means falling into pulverizer 174, which reduces the cuttings to a granular material of about 200 micron size.
  • Screw conveyor 146 is housed in stainless steel pipe unit section 180 which is joined to pulverizer 174 by flange 182.
  • Power screw 146 forces the cuttings into corrosion resistant second stage pipe 182, which is preferably made of high-temperature corrosionresistant chromium-nickel alloy, such as that sold under the name "Inconel”.
  • the cuttings in second stage 136 occupy a relatively narrow gap 154 between shaft 152 and tube 182, where they are raised to a temperature of preferably about 2600°F. (1425.2°C).
  • Second stage 136 causes the residue on and in the cuttings to volatilize completely and to ignite.
  • Second stage 136 is further promoted by introduction of volatilized gases from the first stage which, when mixed with air injected from line 186 cause heating of hollow shaft 152. These gases serve not only to reduce the power requirements needed to maintain the through-heating temperature but also as an ignition additive for gases which are volatilized in second stage 136 and pass into line 178.
  • Cuttings emerging from tube 182 are now powdered and have all oxidizable residue removed, and are then extruded through die block 188.
  • the orifice size through which the product passes is about 0.793mm., although this dimension can be varied.
  • the clean solid material exiting from die block 188 is cooled and consolidated by water from water spray 190 and may be pelletized or otherwise placed into a convenient form for handling. Dust slinger 150 can optionally be provided for disposal of the clean material into a body of water.
  • the device Due to closed loop venting of combustible gases within the system, the device poses little hazard to drilling sites and its straightline design will allow it to be rigged between decks or outboard of a platform of offshore drilling rig, thereby minimizing the space requirements for installation. All major criteria identified as necessary for successful development of a cuttings disposal device have been addressed with the invention forms described. It should be particularly noted that the device is effective with cuttings derived from commonly encountered rock types, including shale characterized by numerous fracture planes in which oil can become embedded. Accordingly, an extremely thorough removal of hydrocarbon materials, even those naturally occurring in the formation rock, can occur.
  • the water soluble constituents of samples 2 and 3 were measured by extracting 25 grams of each sample with 25 milliliters of dionized water, the extract being filtered and analyzed by atomic absorption spectroscopy.
  • the cation exchange capacity of samples 2 and 3 was determined by the methylene blue test.
  • the measured cation exchange capacity of less than 0.1 meq/100 gram of cuttings indicates that the cuttings have been converted to an inert ceramic material by the cuttings cleaner.
  • This test was performed on a slurry of 50 grams ground cuttings per 100 milliliters of deionized water. The slurry was then titrated with methylene blue solution to the end point and the cation exchange capacity calculated.
  • Ignition loss for samples 2 and 3 indicates that oxygen reacted to some of the compounds present in those samples.
  • the moisture content test was performed by drying preweighed samples in porcelain crucibles at 105°C. for 2 hours. The moisture content was calculated, and the samples were then placed in a muffle furnace in an oxidizing atmosphere and heated up to 950°C, being held at that temperature for 2 hours. After cooling, the samples were reweighed and the ignition loss calculated. Results of these tests appear in Table 2.
  • hydrocarbons have, been reduced to below 0.2 parts per million. Further, when mixed with sea water, the cuttings reveal no discernible sheen on the water surface.
  • solid waste materials of miscellaneous types generated at an oil drilling rig site can be mixed with cuttings for disposal with the apparatus of the present invention.
  • sewage, pulverized garbage, and the like on a mobile offshore drilling rig can be handled, thereby affording the capability of handling environmental problems associated with treatment of solid waste generated in the course of operation of an offshore facility.
  • each form of the invention is that no closely spaced moving parts in the high-temperature, second stage area exist, and accordingly, laminar flow of the slow-moving charge of solid materials can serve to reduce the resistance between the material and high-temperature "Inconel" components.
  • the chromium-nickel alloy of the present invention has been found greatly superior to such materials in actual use without the necessity for rebuilding, as is conventionally required.
  • the solid material in the gap appeared to have generated a liquified film 73 on the surfaces of the drum 70 and tube 72 as shown in Fig. 6 which also illustrates the laminar flow of the cuttings.
  • Such a film could account for the high erosion resistance encountered under the conditions of operation of the present apparatus.
  • the gap is about 4.7625mm. in thickness, with successful use of thicknesses up to 15.875mm. However, if the thickness is excessive, improper treatment will result.
  • a virtual explosion-proof device results.
  • a pressure vessel can be constructed around the entire apparatus to provide additional assurance of containing any explosions which could result.

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  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Mining & Mineral Resources (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Fluid Mechanics (AREA)
  • Physics & Mathematics (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Microbiology (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Sustainable Development (AREA)
  • Processing Of Solid Wastes (AREA)
  • Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
  • Shovels (AREA)

Abstract

Dispositif de traitement de boues de débris de forage dans un fluide de forage de puits de pétrole à base d'huile, utilisé généralement dans l'exploitation de puits pétroliers. Les débris possédant un revêtement d'hydrocarbure, après le traitement dans le dispositif sont suffisamment exempts d'hydrocarbures pour pouvoir être déchargés dans un plan d'eau sans créer de problèmes pour l'environnement, tels que la formation d'une pellicule décelable à la surface de l'eau. Un procédé continu à deux étages est utilisé pour élever la température d'une couche relativement mince de fragments rocheux pulvérisés ou autres débris pour effectuer un dégagement en série d'hydrocarbures sous forme gazeuse. Dans le premier étage (12), les fragments rocheux introduits sont envoyés de force dans une région annulaire mince (44) délimitée par une paroi disposée autour (36) et composée d'un métal résistant à la corrosion chauffé à une température à laquelle les produits d'hydrocarbures sont gazéifiés de manière à en permettre l'extraction. Dans le deuxième étage (14), le produit pulvérisé du premier étage (12) est introduit de force dans une région annulaire cylindrique (68) à partir de laquelle on extrait les résidus des produits d'hydrocarbures. Une partie des produits gazeux formés peut être mélangée à de l'air ou de l'oxygène pour permettre la combustion (70) de manière à satisfaire une partie des besoins énergétiques du dispositif.
EP19820900860 1982-01-29 1982-01-29 Procede et dispositif de traitement de debris rocheux de forages. Withdrawn EP0099884A4 (fr)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/US1982/000131 WO1983002568A1 (fr) 1982-01-29 1982-01-29 Procede et dispositif de traitement de debris rocheux de forages

Publications (2)

Publication Number Publication Date
EP0099884A1 true EP0099884A1 (fr) 1984-02-08
EP0099884A4 EP0099884A4 (fr) 1985-07-01

Family

ID=22167794

Family Applications (1)

Application Number Title Priority Date Filing Date
EP19820900860 Withdrawn EP0099884A4 (fr) 1982-01-29 1982-01-29 Procede et dispositif de traitement de debris rocheux de forages.

Country Status (4)

Country Link
EP (1) EP0099884A4 (fr)
AU (1) AU8207882A (fr)
NO (1) NO830526L (fr)
WO (1) WO1983002568A1 (fr)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2526087B (en) * 2014-05-12 2020-08-19 Dps Bristol Holdings Ltd Waste treatment process for a fossil-fuel extraction site
GB2527829A (en) 2014-07-03 2016-01-06 Dps Bristol Holdings Ltd A gasifier

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3570420A (en) * 1970-05-07 1971-03-16 Michem Inc Process for the removal of hydrocarbons contained in earth cuttings from subterranean wells
US3658015A (en) * 1970-04-15 1972-04-25 Dresser Ind Explosive-proof method and incinerator for burning drill cuttings

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
USRE26352E (en) * 1968-02-20 Apparatus and process for uhiynrating waste solids concentrates
US3211209A (en) * 1962-10-16 1965-10-12 Monsanto Co Apparatus for changing the volatile content of viscous materials
US3242969A (en) * 1963-01-31 1966-03-29 Braun & Co C F Polymer desolventizer of the rotary wiped falling film type
US3812897A (en) * 1971-08-11 1974-05-28 Monsanto Co Wiped film devolatilization process
US3780676A (en) * 1972-05-08 1973-12-25 Air Preheater Metallic recovery system

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3658015A (en) * 1970-04-15 1972-04-25 Dresser Ind Explosive-proof method and incinerator for burning drill cuttings
US3570420A (en) * 1970-05-07 1971-03-16 Michem Inc Process for the removal of hydrocarbons contained in earth cuttings from subterranean wells

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of WO8302568A1 *

Also Published As

Publication number Publication date
WO1983002568A1 (fr) 1983-08-04
EP0099884A4 (fr) 1985-07-01
AU8207882A (en) 1983-08-12
NO830526L (no) 1983-08-04

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