EP3431910B1 - Countercurrent-type direct heating heat exchanger - Google Patents

Countercurrent-type direct heating heat exchanger Download PDF

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Publication number
EP3431910B1
EP3431910B1 EP17766831.6A EP17766831A EP3431910B1 EP 3431910 B1 EP3431910 B1 EP 3431910B1 EP 17766831 A EP17766831 A EP 17766831A EP 3431910 B1 EP3431910 B1 EP 3431910B1
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EP
European Patent Office
Prior art keywords
flow guide
ore slurry
heat exchanger
umbrella
container
Prior art date
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Application number
EP17766831.6A
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German (de)
English (en)
French (fr)
Other versions
EP3431910A4 (en
EP3431910A1 (en
Inventor
Yuta Uchida
Takashi Sakamoto
Yoji Kyoda
Osamu Nakai
Satoshi Matsubara
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Sumitomo Metal Mining Co Ltd
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Sumitomo Metal Mining Co Ltd
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Publication of EP3431910A1 publication Critical patent/EP3431910A1/en
Publication of EP3431910A4 publication Critical patent/EP3431910A4/en
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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
    • F28C3/00—Other direct-contact heat-exchange apparatus
    • F28C3/06—Other direct-contact heat-exchange apparatus the heat-exchange media being a liquid and a gas or vapour
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F25/00—Component parts of trickle coolers
    • F28F25/02—Component parts of trickle coolers for distributing, circulating, and accumulating liquid
    • F28F25/08—Splashing boards or grids, e.g. for converting liquid sprays into liquid films; Elements or beds for increasing the area of the contact surface
    • C—CHEMISTRY; METALLURGY
    • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B23/00—Obtaining nickel or cobalt
    • C22B23/04—Obtaining nickel or cobalt by wet processes
    • C22B23/0407—Leaching processes
    • C22B23/0415—Leaching processes with acids or salt solutions except ammonium salts solutions
    • C22B23/043—Sulfurated acids or salts thereof
    • C—CHEMISTRY; METALLURGY
    • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B23/00—Obtaining nickel or cobalt
    • C22B23/04—Obtaining nickel or cobalt by wet processes
    • C22B23/0453—Treatment or purification of solutions, e.g. obtained by leaching
    • C22B23/0461—Treatment or purification of solutions, e.g. obtained by leaching by chemical methods
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/22—Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
    • F28F2009/222—Particular guide plates, baffles or deflectors, e.g. having particular orientation relative to an elongated casing or conduit
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2265/00—Safety or protection arrangements; Arrangements for preventing malfunction
    • F28F2265/06—Safety or protection arrangements; Arrangements for preventing malfunction by using means for draining heat exchange media from heat exchangers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2265/00—Safety or protection arrangements; Arrangements for preventing malfunction
    • F28F2265/22—Safety or protection arrangements; Arrangements for preventing malfunction for draining
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F25/00—Component parts of trickle coolers
    • F28F25/02—Component parts of trickle coolers for distributing, circulating, and accumulating liquid
    • F28F25/06—Spray nozzles or spray pipes

Definitions

  • This invention relates to a countercurrent direct-heating heat exchanger. More specifically, this invention relates to a countercurrent direct-heating heat exchanger that exchanges heat by making a heating target fluid and a heating medium contact each other directly while flowing the heating target fluid into the heat exchanger from an upper part thereof and flowing the heating target fluid out of the heat exchanger from a lower part thereof, and simultaneously, flowing the heating medium into the heat exchanger from a lower part thereof and flowing the heating medium out of the heat exchanger from an upper part thereof.
  • High-temperature and pressure sulfuric acid leaching which is high pressure acid leaching (HPAL) using sulfuric acid
  • HPAL high pressure acid leaching
  • hydrometallurgy to recover a valuable metal such as nickel or cobalt, etc. from a low-grade nickel oxide ore represented by a limonite ore, etc.
  • Hydrometallurgy by means of high-temperature and pressure sulfuric acid leaching includes a pretreatment step and a high-temperature and pressure sulfuric acid leaching step.
  • a nickel oxide ore is crushed and classified to manufacture an ore slurry.
  • the high-temperature and pressure sulfuric acid leaching step the ore slurry is charged into an autoclave and then leaching process is performed under a leaching condition such as a temperature or a pressure selected, as necessary.
  • a temperature from about 200 to about 300°C is generally selected as a condition for leaching in the autoclave.
  • the ore slurry manufactured in the pretreatment step is placed at a temperature substantially the same as an outside air temperature.
  • charging the ore slurry at this temperature as it is into the autoclave not only reduces a temperature in the autoclave to reduce a leaching rate but also causes an unstable temperature condition to make it difficult to produce stable leaching reaction.
  • a responsive method having been employed is to make the temperature of the ore slurry approach a temperature in the autoclave by preheating the ore slurry and then charge the preheated ore slurry into the autoclave.
  • a countercurrent direct-heating heat exchanger is used as a preheating facility for an ore slurry (patent literature 1).
  • the countercurrent direct-heating heat exchanger exchanges heat by making a heating target fluid (ore slurry) and a heating medium (water vapor) contact each other directly while flowing the heating target fluid into the heat exchanger from an upper part thereof and flowing the heating target fluid out of the heat exchanger from a lower part thereof, and simultaneously, flowing the heating medium into the heat exchanger from a lower part thereof and flowing the heating medium out of the heat exchanger from an upper part thereof.
  • Patent Literature 1 Japanese Patent Application Publication No. 2010-25455 .
  • This document discloses in figures 1 to 4 a countercurrent direct-heating heat exchanger comprising: a container; a supply pipe through which a heating target fluid is supplied into the container; an inlet provided at an end portion of the supply pipe; a flow guide connected to the inlet and guiding the heating target fluid to flow in a vertically downward direction; and an umbrella-shape distribution plate having a top arranged vertically below the flow guide, wherein the flow guide includes a cylindrical body.
  • Using the countercurrent direct-heating heat exchanger for hearing an ore slurry may cause wear of the side wall of a container of the countercurrent direct-heating heat exchanger by the ore slurry.
  • this invention is intended to provide a countercurrent direct-heating heat exchanger capable of suppressing wear of a container caused by a heating target fluid.
  • a countercurrent direct-heating heat exchanger includes: a container; a supply pipe through which a heating target fluid is supplied into the container; an inlet provided at an end portion of the supply pipe; a flow guide connected to the inlet and guiding the heating target fluid to flow in a vertically downward direction; and an umbrella-shape distribution plate having a top arranged vertically below the flow guide.
  • the flow guide includes: a cylindrical body; and a partitioning member that partitions the interior of the cylindrical body into a plurality of flow paths extending along the center axis of the cylindrical body.
  • the countercurrent direct-heating heat exchanger according to the invention further comprises a slit formed at the cylindrical body, the partitioning member including an insertion plate, and the insertion plate being inserted into the slit and the slit and the inserted insertion plate being welded.
  • the countercurrent direct-heating heat exchanger according to a first embodiment of the invention is characterized in the flow guide includes a blocking member arranged on the center axis of the flow guide and blocking the flow of the heating target fluid.
  • the countercurrent direct-heating heat exchanger according to a second embodiment of the invention is characterized in that the umbrella-shape distribution plate is covered by a sacrificial member at the top and the vicinity of the top.
  • the countercurrent direct-heating heat exchanger according to a third embodiment of the invention is characterized in that the flow guide is connected in a removable manner to the inlet.
  • the countercurrent direct-heating heat exchanger according to a fourth embodiment of the invention is characterized in that a distance between an opening of the flow guide and the top of the umbrella-shape distribution plate is from 1. 1 to 1.3 times the diameter of the flow guide.
  • the countercurrent direct-heating heat exchanger according to a fifth embodiment of the invention is characterized in that the supply pipe is arranged substantially horizontally.
  • the countercurrent direct-heating heat exchanger according to a sixth embodiment of the invention is characterized in that the heating target fluid is a slurry.
  • the flow guide can suppress deflection of the heating target fluid.
  • the heating target fluid flows down to the top or the vicinity of the top of the umbrella-shape distribution plate and is distributed uniformly in all directions of the umbrella-shape distribution plate.
  • the amount of the heating target fluid to contact the side wall of the container is not increased locally to allow suppression of the wear of the container caused by the heating target fluid.
  • the tight joint by welding between the cylindrical body and the partitioning member can function to stand against resistance produced by the flow of the heating target fluid to reduce the probability of damage of the flow guide.
  • the flow velocity of the heating target fluid vertically below the blocking member is restricted.
  • collision of the heating target fluid with the top of the umbrella-shape distribution plate can be weakened to allow reduction in damage of the umbrella-shape distribution plate.
  • the sacrificial member receives impact caused by flowing down of the heating target fluid. In this way, wear of the umbrella-shape distribution plate can be suppressed.
  • the flow guide as the flow guide is removable, the flow guide can be exchanged or repaired easily.
  • the distance between the flow guide and the umbrella-shape distribution plate is 1. 1 times the diameter of the flow guide or more. This causes the heating target fluid to flow smoothly to weaken rubbing between the heating target fluid and the umbrella-shape distribution plate. Thus, wear of the umbrella-shape distribution plate can be suppressed.
  • the distance between the flow guide and the umbrella-shape distribution plate does not exceed 1.3 times the diameter of the flow guide. Thus, a direction in which the heating target fluid flows down from the flow guide is unlikely to be changed by the flow of a heating medium.
  • the flow guide can still guide the heating target fluid to flow in a vertically downward direction.
  • the heating target fluid is a slurry
  • wear of the container caused by the heating target fluid can still be suppressed.
  • a countercurrent direct-heating heat exchanger A is used for hydrometallurgy to obtain nickel-cobalt mixed sulfide from a nickel oxide ore using high-temperature and pressure sulfuric acid leaching.
  • the hydrometallurgy includes a pretreatment step (101), a high-temperature and pressure sulfuric acid leaching step (102), a solid-liquid separating step (103), a neutralizing step (104), a dezincification step (105), a sulfurizing step (106), and a detoxifying step (107).
  • An ore to be used as a nickel oxide ore as a raw material is mainly what is called a laterite ore such as a limonite ore and a saprolite ore, for example.
  • a nickel content in the laterite ore is generally from 0.5 to 3.0% by mass.
  • the laterite ore contains nickel in the form of hydroxide or a siliceous magnesia (magnesium silicate) ore.
  • An iron content in the laterite ore is from 10 to 50% by mass.
  • the laterite ore contains iron mainly in the form of trivalent hydroxide (goethite, FeOOH) and partially in the form of divalent iron as a magnesium silicate ore.
  • the nickel oxide ore is crushed, classified into an average particle size of 2 mm or less, and then slurried to manufacture an ore slurry. Redundant water in the ore slurry is removed using a solid-liquid separating device such as a thickener to concentrate the ore slurry so as to obtain a predetermined concentration of a solid in the ore slurry.
  • a solid-liquid separating device such as a thickener to concentrate the ore slurry so as to obtain a predetermined concentration of a solid in the ore slurry.
  • sulfuric acid is added to the ore slurry obtained in the pretreatment step (101). Then, the ore slurry is agitated under a temperature condition from 200 to 300°C for high-temperature and pressure acid leaching, thereby obtaining a leached slurry.
  • the leached slurry obtained in the high-temperature and pressure sulfuric acid leaching step (102) is separated into a solid and a liquid to obtain a leachate containing nickel and cobalt (hereinafter called a "crude nickel sulfate solution”) and a leaching residue.
  • a leachate containing nickel and cobalt hereinafter called a "crude nickel sulfate solution”
  • the neutralizing step (104) the crude nickel sulfate solution obtained in the solid-liquid separating step (103) is neutralized.
  • hydrogen sulfide gas is added to the crude nickel sulfate solution neutralized in the neutralizing step (104) to remove zinc as a precipitate of zinc sulfide.
  • the sulfurizing step (106) hydrogen sulfide gas is added to final solution resulting from the dezincification obtained in the dezincification step (105) to obtain nickel-cobalt mixed sulfide and nickel barren solution.
  • the detoxifying step (107) the leaching residue generated in the solid-liquid separating step (103) and the nickel barren solution generated in the sulfurizing step (106) are detoxified.
  • a solid concentration in the ore slurry (weight ratio of a solid (ore) in the slurry) manufactured in the pretreatment step (101) depends largely on the properties of the nickel oxide ore as a raw material.
  • the concentration of a solid in the ore slurry is controlled in such a manner that the solid represents from 20 to 50% by mass. If a concentration in the ore slurry is less than 20% by mass, a large facility should be prepared for obtaining given time of stay during leaching and the amount of acid to be added should be increased for adjusting a residual acid concentration. Additionally, a nickel concentration in a resultant leachate is reduced.
  • the high-temperature and pressure sulfuric acid leaching step (102) includes two sub-steps (a preheating step and a leaching step).
  • the preheating step the ore slurry at a temperature about an outside air temperature carried from the pretreatment step (101) is preheated to make the temperature of the ore slurry approach a temperature in an autoclave to be used in the leaching step.
  • the leaching step the ore slurry carried from the preheating step is charged into the autoclave. Then, leaching is performed by adding sulfuric acid to the ore slurry and blowing high-pressure air and high-pressure water vapor into the autoclave.
  • the countercurrent direct-heating heat exchanger A of this embodiment is used for heating the ore slurry in the preheating step. If necessary, two or more countercurrent direct-heating heat exchangers A are connected in series and the ore slurry is heated in stages.
  • the countercurrent direct-heating heat exchanger A uses water vapor as a heating medium.
  • Water vapor to be used may be generated by using a common method such as a boiler.
  • pressure is reduced in stages using a pressure reducing container. Water vapor generated in this pressure reducing container may be collected and used as a heating medium in the countercurrent direct-heating heat exchanger A.
  • the countercurrent direct-heating heat exchanger A is a heat exchanger that exchanges heat by flowing a heating target fluid 1 and a heating medium 2 in opposite directions and making the heating target fluid 1 and the heating medium 2 contact each other directly.
  • the heating target fluid 1 is an ore slurry 1 obtained in the pretreatment step (101) of the foregoing hydrometallurgy and the heating medium 2 is water vapor 2.
  • the countercurrent direct-heating heat exchanger A includes a substantially circular cylindrical container 10.
  • the container 10 is arranged vertically in such a manner that the center axis of the container 10 extends in the vertical direction.
  • the container 10 is provided with a supply pipe 11 arranged substantially horizontally at an upper part of the container 10.
  • a heating target fluid inlet 12 is provided at an end portion of the supply pipe 11 to be pointed vertically downwardly.
  • a flow guide 40 is connected to the heating target fluid inlet 12.
  • the container 10 is provided with a heating target fluid outlet 13 arranged at a lower part, more specifically, at the bottom of the container 10.
  • the ore slurry 1 as the heating target fluid 1 is supplied into the container 10 through the supply pipe 11, passes through the heating target fluid inlet 12, and flows down from an opening (lower end) of the flow guide 40. Then, the ore slurry 1 flows down in the container 10 and is ejected to the outside of the container 10 from the heating target fluid outlet 13.
  • the heating target fluid inlet 12 corresponds to an "inlet” recited in the appended claims.
  • the heating target fluid inlet 12 will simply be called an inlet 12.
  • the container 10 is provided with a heating medium inlet 14 arranged at a lower side wall of the container 10.
  • the container 10 is provided with a heating medium outlet 15 arranged at an upper part, more specifically, at the top of the container 10.
  • the water vapor 2 as the heating medium 2 is supplied from the heating medium inlet 14 into the container 10.
  • the supplied water vapor 2 moves up in the container 10 and is then ejected to the outside of the container 10 from the heating medium outlet 15.
  • Dashed arrows of Fig. 1 show a flow of the water vapor 2.
  • the container 10 is provided with a plurality of umbrella-shape distribution plates 20 and a plurality of annular flow guide plates 30.
  • the umbrella-shape distribution plates 20 and the annular flow guide plates 30 are arranged alternately, one above the other, with the respective centers being substantially aligned with each other.
  • These umbrella-shape distribution plates 20 and these annular flow guide plates 30 each have a tilted surface.
  • the ore slurry 1 supplied into the container 10 flows down along the respective tilted surfaces of the umbrella-shape distribution plates 20 and those of the annular flow guide plates 30 to drop down from downstream edge portions of the tilted surfaces. By making this flow repeatedly, the ore slurry 1 flows down in the container 10. Meanwhile, the water vapor 2 supplied into the container 10 moves up in the container 10 while passing through between the umbrella-shape distribution plates 20 and the annular flow guide plates 30 in a zigzag manner.
  • the supply pipe 11 is arranged to extend in the direction of the diameter of the container 10 from the side wall to a substantially central point of the container 10.
  • the inlet 12 is formed at an end portion of the supply pipe 11.
  • the inlet 12 is arranged at a substantially central point of the container 10 in a plan view.
  • the flow guide 40 is also arranged at a substantially central point of the container 10 in a plan view.
  • the supply pipe 11 is supported by a beam 11a extending linearly from the end portion of the supply pipe 11 to the side wall of the container 10.
  • the umbrella-shape distribution plate 20 is a tilted plate having an umbrella shape (conical shape).
  • the umbrella-shape distribution plate 20 is arranged in such a manner that the top of the umbrella-shape distribution plate 20 is pointed upwardly and the top (center) substantially agrees with the center of the container 10 in a plan view.
  • the top of the umbrella-shape distribution plate 20 is arranged vertically below the flow guide 40.
  • the ore slurry 1 is supplied from the flow guide 40 to the top of the umbrella-shape distribution plate 20 in a top layer, distributed radially along the tilted surface of the umbrella-shape distribution plate 20, and drops down in a skirt-like manner from a downstream edge portion 21.
  • the downstream edge portion 21 of the umbrella-shape distribution plate 20 is an edge where the side surface and the bottom surface of a cone contact each other.
  • the umbrella-shape distribution plate 20 in the top layer is covered by a sacrificial member 22 at the top and the vicinity of the top.
  • the sacrificial member 22 may be formed by hardfacing or using a material having a strength such as a steel sheet.
  • the annular flow guide plate 30 is an annular tilted plate having a slope descending from the outer peripheral edge toward the inner peripheral edge of the annular flow guide plate 30.
  • the outer diameter of the annular flow guide plate 30 is substantially the same as the inner diameter of the container 10.
  • the outer peripheral edge of the annular flow guide plate 30 contacts the inner wall of the container 10.
  • the annular flow guide plate 30 is arranged in such a manner that the center of the annular flow guide plate 30 (the respective centers of the outer periphery and the inner periphery) substantially agrees with the center of the container 10 in a plan view.
  • the ore slurry 1 After dropping down from the umbrella-shape distribution plate 20 to the annular flow guide plate 30, the ore slurry 1 flows down along the tilted surface toward the center of the annular flow guide plate 30 and then drops down in a skirt-like manner from a downstream edge portion 31.
  • the downstream edge portion 31 of the annular flow guide plate 30 is the inner peripheral edge thereof.
  • the ore slurry 1 is supplied into the container 10 from the flow guide 40.
  • the ore slurry 1 supplied into the container 10 first flows down radially along the tilted surface of the umbrella-shape distribution plate 20 in the top layer and then drops down in a skirt-like manner from the downstream edge portion 21.
  • the ore slurry 1 flows down along the tilted surface toward the center of the annular flow guide plate 30 and then drops down in a skirt-like manner from the downstream edge portion 31. Then, the ore slurry 1 drops down to the umbrella-shape distribution plate 20 in a subsequent layer.
  • the ore slurry 1 flows down along the respective tilted surfaces of the umbrella-shape distribution plate 20 and the annular flow guide plate 30 alternately and is then ejected to the outside of the container 10 from the heating target fluid outlet 13 at the lower part of the container 10.
  • the water vapor 2 is supplied into the container 10 from the heating medium inlet 14 at the lower part of the container 10, moves up while passing through between the umbrella-shape distribution plate 20 and the annular flow guide plate 30 in a zigzag manner, and is then ejected to the outside of the container 10 from the heating medium outlet 15 at the upper part of the container 10.
  • the water vapor 2 contacts the ore slurry 1 directly by flowing along the ore slurry 1 while the ore slurry 1 flows down along the respective tilted surfaces of the umbrella-shape distribution plate 20 and the annular flow guide plate 30.
  • the water vapor 2 also contacts the ore slurry 1 directly by passing through the ore slurry 1 while the ore slurry 1 drops down from the downstream edge portions 21 and 31 of the umbrella-shape distribution plate 20 and the annular flow guide plate 30 respectively. In this way, heat is exchanged between the ore slurry 1 and the water vapor 2.
  • the countercurrent direct-heating heat exchanger A exchanges heat by making the ore slurry 1 and the water vapor 2 contact each other directly while flowing the ore slurry 1 into the heat exchanger A from an upper part thereof and flowing the ore slurry 1 out of the heat exchanger A from a lower part thereof, and simultaneously, flowing the water vapor 2 into the heat exchanger A from a lower part thereof and flowing the water vapor 2 out of the heat exchanger A from an upper part thereof.
  • the ore slurry 1 is distributed radially along the umbrella-shape distribution plate 20. This increases an area of contact between the ore slurry 1 and the water vapor 2 to increase heat exchange efficiency. Further, the flow of the water vapor 2 is guided along the annular flow guide plate 30 and the water vapor 2 flows along the ore slurry 1 while the ore slurry 1 flows down along the tilted surface of the umbrella-shape distribution plate 20. This also increases an area of contact between the ore slurry 1 and the water vapor 2 to increase heat exchange efficiency.
  • Fig. 5 is an enlarged view showing the inlet 12 and its vicinity in the absence of the flow guide 40. Alternate long and two short dashes lines O in Fig. 5 show a vertical line passing through the center of the inlet 12.
  • the ore slurry 1 flows in a substantially horizontal direction in the supply pipe 11 and then flows down from the inlet 12.
  • the ore slurry 1 is under the force of gravity while flowing down from the inlet 12, so that the ore slurry 1 flows in a direction downward from the horizontal direction.
  • the ore slurry 1 still has momentum in the horizontal direction generated during the flow of the ore slurry 1 in the supply pipe 11.
  • a direction in which the ore slurry 1 flows down from the inlet 12 is tilted from a vertically downward direction.
  • the ore slurry 1 is tilted in a direction in which the supply pipe 11 extends (leftward direction of Fig. 5 ).
  • a phenomenon where such a tilt of the flow direction of the ore slurry 1 from the vertically downward direction occurs when the ore slurry 1 flows down from the inlet 12 is called "deflection."
  • a part of the ore slurry 1 flowing along the tilted surface of the umbrella-shape distribution plate 20 and flowing in the direction of the deflection has greater momentum than a part of the ore slurry 1 flowing in a different direction.
  • This part of the ore slurry 1 having greater momentum drops down from the downstream edge portion 21 of the umbrella-shape distribution plate 20 and then contacts the side wall of the container 10.
  • a part of the side wall of the container 10 located in the direction of the deflection (part w of Fig. 1 ) is to contact the ore slurry 1 of a greater amount than a different part of the side wall.
  • the amount of the ore slurry 1 to contact the side wall of the container 10 is increased locally.
  • the part of the side wall of the container 10 (part w) is more likely to be worn out by the ore slurry 1 than a different part.
  • the ore slurry 1 is not distributed uniformly in all directions of the umbrella-shape distribution plate 20 to cause imbalance. As a result, heat exchange efficiency is reduced.
  • a deflection angle ⁇ (an angle formed between a direction in which the ore slurry 1 flows and a vertical line O) changes in a manner that depends on the flow rate of the ore slurry 1, a slurry specific gravity, or a solid concentration. These parameters change during operation of the countercurrent direct-heating heat exchanger A.
  • the deflection angle ⁇ changes during the operation to change a position where the ore slurry 1 having flowed down from the inlet 12 collides with the umbrella-shape distribution plate 20. Apart of the umbrella-shape distribution plate 20 to collide with the ore slurry 1 having flowed down from the inlet 12 is likely to be damaged. If the deflection angle ⁇ changes during the operation, flowing down of the ore slurry 1 may cause impact on a wide range of the umbrella-shape distribution plate 20. It is difficult to protect the umbrella-shape distribution plate 20 from such impact.
  • the flow guide 40 is attached to the inlet 12.
  • the flow guide 40 has the function of guiding the ore slurry 1 to flow in a vertically downward direction.
  • the flow guide 40 is constructed of a cylindrical body 41, a partitioning member 42, and a blocking member 43.
  • the cylindrical body 41 is a member having a circular cylindrical shape and includes a flange 41f at an upper end portion thereof.
  • the flange 41f and a flange 12f of the inlet 12 are coupled with a bolt, a nut, etc., thereby attaching the flow guide 40 to the inlet 12.
  • the cylindrical body 41 is formed with four slits 41s each extending from the lower end toward a point near the vertical center of the cylindrical body 41.
  • the slits 41s are formed at regular intervals (at intervals of 90 degrees) in the peripheral direction of the cylindrical body 41.
  • the partitioning member 42 is constructed of a pipe 42a of a small diameter, and eight partitioning plates 42b joined to the outer periphery of the pipe 42a.
  • the partitioning plates 42b are arranged at regular intervals (at intervals of 45 degrees) in the peripheral direction of the pipe 42a.
  • the eight partitioning plates 42b are arranged in a radial pattern about the pipe 42a.
  • the pipe 42a is arranged in such a manner that the center axis of the pipe 42a agrees with a center axis O of the flow guide 40.
  • the partitioning plates 42b are flat plates and arranged to extend along the center axis O.
  • partitioning plates 42b have outer edge portions protruding from their lower ends toward their vertically central points. These protruding portions are called insertion plates 42c.
  • the partitioning plates 42b with the insertion plates 42c and the partitioning plates 42b without the insertion plates 42c are arranged alternately. Specifically, the insertion plates 42c are arranged at intervals of 90 degrees in the peripheral direction of the pipe 42a.
  • the blocking member 43 is a member having a circular plate shape and has a diameter substantially the same as the outer diameter of the pipe 42a.
  • the blocking member 43 is arranged on the center axis O of the flow guide 40 and joined to the upper end of the pipe 42a.
  • the upper end of the pipe 42a is sealed by the blocking member 43.
  • the flow of the ore slurry 1 is blocked in a part in which the blocking member 43 is arranged.
  • the flow of the ore slurry 1 is blocked at the center axis O and its vicinity of the flow guide 40.
  • the flow guide 40 is assembled by the following procedure. First, the partitioning member 42 is inserted from a lower opening of the cylindrical body 41. At this time, the insertion plates 42c of the partitioning member 42 are inserted into the slits 41s of the cylindrical body 41. Then, the slits 41s and the insertion plates 42c are welded.
  • the cylindrical body 41 and the partitioning member 42 are tightly joined by welding. If the ore slurry 1 passes through in the flow guide 40, resistance (friction or impact) acts between the ore slurry 1 and the partitioning member 42 to produce force of pressing the partitioning member 42 downwardly. Meanwhile, the tight joint between the cylindrical body 41 and the partitioning member 42 can function to stand against the downwardly acting force produced by the flow of the ore slurry 1, reducing the probability of damage of the flow guide 40.
  • the foregoing method is not a limited method of assembling the flow guide 40.
  • a configuration of inserting the insertion plates 42c into the slits 41s may not be employed.
  • the flow guide 40 may be assembled simply by welding the inner surface of the cylindrical body 41 and the outer edge portions of the partitioning plates 42b.
  • the cylindrical body 41 and the partitioning member 42 may be fixed by a different method such as fastening with a screw.
  • the interior of the cylindrical body 41 is partitioned into eight flow paths 44 by the partitioning member 42.
  • Both the pipe 42a and the partitioning plates 42b are arranged to extend along the center axis O, so that each flow path 44 extends along the center axis O.
  • the ore slurry 1 flows in a distributed manner through the plurality of flow paths 44 extending along the center axis O of the flow guide 40. This makes it possible to guide the ore slurry 1 to flow in a direction along the center axis O of the flow guide 40.
  • the flow guide 40 is arranged in such a manner that the center axis O of the flow guide 40 substantially agrees with the vertical line passing through the center of the inlet 12.
  • the inlet 12 is arranged at the substantially central point of the container 10, so that the center axis O of the flow guide 40 also substantially agrees with the center axis of the container 10.
  • the deflection of the ore slurry 1 can be suppressed.
  • the ore slurry 1 flows down to the top or the vicinity of the top of the umbrella-shape distribution plate 20 in the top layer and is distributed uniformly in all directions of the umbrella-shape distribution plate 20. This prevents the momentum of the ore slurry 1 flowing along the tilted surface of the umbrella-shape distribution plate 20 from increasing locally.
  • the amount of the ore slurry 1 to contact the side wall of the container 10 is not increased locally to allow suppression of the wear of the container 10 caused by the ore slurry 1.
  • the ore slurry 1 is distributed uniformly in all directions of the umbrella-shape distribution plate 20. This increases the heat exchange efficiency of the countercurrent direct-heating heat exchanger A.
  • the blocking member 43 is provided on the center axis O of the flow guide 40.
  • the top of the umbrella-shape distribution plate 20 is arranged vertically below the blocking member 43.
  • the flow rate (flow velocity) of the ore slurry 1 vertically below the blocking member 43 can be restricted.
  • collision of the ore slurry 1 with the top of the umbrella-shape distribution plate 20 in the top layer can be weakened to allow reduction in damage of the umbrella-shape distribution plate 20.
  • the flow guide 40 causes the ore slurry 1 to pass through, so that the flow guide 40 is worn out easily. After long-time use of the flow guide 40, the flow guide 40 should be exchanged or repaired.
  • the flow guide 40 is attached to the inlet 12 at the flange 41f as described above, so that the flow guide 40 is removable. As the flow guide 40 is removable, even if the flow guide 40 is worn out, the flow guide 40 can be exchanged or repaired easily.
  • a distance H between the opening at the lower end of the flow guide 40 and the top of the umbrella-shape distribution plate 20 in the top layer is preferably from 1. 1 to 1.3 times a diameter D of the flow guide 40.
  • the ore slurry 1 is accumulated at an exit of the flow guide 40. In this case, the ore slurry 1 rubs vigorously against the umbrella-shape distribution plate 20. As a result, the umbrella-shape distribution plate 20 becomes likely to be worn out easily. Further, by the presence of the accumulated ore slurry 1, the ore slurry 1 in the flow guide 40 is decelerated to cause the risk of blockage of the flow guide 40 by the ore slurry 1. If the distance H is 1.1 times the diameter D or more, the ore slurry 1 is caused to flow smoothly to weaken rubbing between the ore slurry 1 and the umbrella-shape distribution plate 20. Thus, wear of the umbrella-shape distribution plate 20 can be suppressed.
  • the ore slurry 1 having flowed down from the flow guide 40 is disturbed by the flow of the water vapor 2 to cause the risk of failing to maintain uniform distribution at the umbrella-shape distribution plate 20. Additionally, if the ore slurry 1 of a large amount exceeding the capability of the flow guide 40 to guide a flow is supplied, the ore slurry 1 may collide with the side wall of the container 10 directly without abutting on the umbrella-shape distribution plate 20. If the distance H does not exceed 1.3 times the diameter D, a direction in which the ore slurry 1 flows down from the flow guide 40 is unlikely to be changed by the flow of the water vapor 2. Further, the ore slurry 1 does not collide with the side wall of the container 10 directly.
  • An opening surface of the flow guide 40 is perpendicular to the center axis O.
  • the partitioning member 42 may be formed by tying a plurality of small-diameter pipes 42d together.
  • the cross section of the small-diameter pipe 42d is not limited to a circular shape but may be a polygonal shape.
  • the partitioning member 42 may be formed by combining a plurality of partitioning plates 42e in a radial pattern.
  • the number of the flow paths 44 in the cylindrical body 41 is not limited to eight but is required to be two or more. If the partitioning member 42 formed by combining the partitioning plates 42e in a cross shape is used, four flow paths 44 are formed.
  • Adjacent flow paths 44 may be partitioned completely by the partitioning member 42.
  • the partitioning member 42 may include a communication part for making communication between the adjacent flow paths 44.
  • the blocking member 43 is required to be arranged on the center axis O of the flow guide 40. If the blocking member 43 having a circular plate shape is used, the upper part of the flow guide 40 is not a limited place for arrangement of the blocking member 43 but the blocking member 43 may be arranged at a lower part or a vertically central part of the flow guide 40.
  • the shape of the blocking member 43 is not limited to a circular plate shape but various shapes are applicable.
  • the blocking member 43 may have a circular columnar shape or a conical shape.
  • the conical blocking member 43 is assembled into the partitioning member 42 with the top of the blocking member 43 pointed upwardly. This causes the ore slurry 1 to flow along a tilted surface of the blocking member 43. In this way, collision of the ore slurry 1 with the blocking member 43 and resultant dispersion of the ore slurry 1 can be suppressed.
  • the heating target fluid 1 is not particularly limited but is required to be a heating target having flowability.
  • the heating target fluid 1 may be liquid with flowability in the form of a slurry containing a solid component.
  • the liquid with flowability in the form of a slurry may be a slurry (ore slurry) containing an ore.
  • the ore slurry may be a slurry containing a nickel oxide ore obtained in the pretreatment step (101) of the hydrometallurgy, for example. Even if the heating target fluid 1 is a slurry, wear of the container 10 caused by the heating target fluid 1 can still be suppressed.
  • the heating medium 2 is not particularly limited but is required to be a medium to supply heat to the heating target fluid 1.
  • the heating medium 2 may be gas such as water vapor at a higher temperature than the heating target fluid 1.
  • Figs. 6A and 6B The shape of the flow guide 40 shown in Figs. 6A and 6B was employed.
  • Fig. 10A shows the concentration distribution of the slurry.
  • Fig. 10B shows the flow velocity distribution of the slurry.
  • the concentration of the slurry is uniform and the slurry is distributed uniformly in all directions of the umbrella-shape distribution plate 20.
  • the flow velocity of the slurry flowing down from the flow guide 40 is lower at the center and its vicinity than at an external point. This results from effect brought by the blocking member 43. The flow velocity of the slurry is found to be restricted at the top of the umbrella-shape distribution plate 20.
  • the countercurrent direct-heating heat exchanger has the same basic configuration as the countercurrent direct-heating heat exchanger A shown in Fig. 1 .
  • the side wall of the container 10 of the countercurrent direct-heating heat exchanger is made of titanium of a thickness of 9 mm on an inner side and carbon steel of a thickness of 23.5 mm on an outer side.
  • the side wall has a total thickness of 32.5 mm.
  • the flow guide 40 shown in Figs. 6A and 6B was attached to the inlet 12.
  • the ore slurry 1 was supplied to the countercurrent direct-heating heat exchanger and operation was started.
  • the state of the interior of the countercurrent direct-heating heat exchanger was checked one year after start of the operation and no thickness reduction of the side wall of the container 10 was found.
  • the state of the interior of the countercurrent direct-heating heat exchanger was checked two years after start of the operation and no thickness reduction of the side wall of the container 10 was found.
  • the flow guide 40 used in Working Example 1 was replaced by a short pipe.
  • the short pipe has dimensions similar to those of the cylindrical body 41 of the flow guide 40.
  • the other conditions are the same as those of Working Example 1.
  • the state of the interior of the countercurrent direct-heating heat exchanger was checked one year after start of the operation and thickness reduction of the side wall of the container 10 was found.
  • the state of the interior of the countercurrent direct-heating heat exchanger was checked two years after start of the operation and a pin hole appeared in the side wall of the container 10 due to further development of the thickness reduction.
  • Working Example 1 was found to be capable of suppressing wear of the side wall of the container 10. This is considered to be realized by the uniform flow of the ore slurry 1 in all directions of the umbrella-shape distribution plate 20 as a result of provision of the flow guide 40.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)
EP17766831.6A 2016-03-18 2017-03-17 Countercurrent-type direct heating heat exchanger Active EP3431910B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2016054629A JP6631346B2 (ja) 2016-03-18 2016-03-18 向流式直接加熱型熱交換器
PCT/JP2017/010832 WO2017159836A1 (ja) 2016-03-18 2017-03-17 向流式直接加熱型熱交換器

Publications (3)

Publication Number Publication Date
EP3431910A1 EP3431910A1 (en) 2019-01-23
EP3431910A4 EP3431910A4 (en) 2019-12-04
EP3431910B1 true EP3431910B1 (en) 2020-09-30

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EP (1) EP3431910B1 (ja)
JP (1) JP6631346B2 (ja)
AU (1) AU2017232774B9 (ja)
CU (1) CU20180099A7 (ja)
PH (1) PH12018501730A1 (ja)
WO (1) WO2017159836A1 (ja)

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CN108506957A (zh) * 2018-07-05 2018-09-07 北京蓝爱迪电力技术有限公司 一种锅炉燃用煤粉加热设备

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JPS5414593B2 (ja) * 1974-06-08 1979-06-08
JPH0284870U (ja) * 1988-12-16 1990-07-02
JPH03275824A (ja) * 1990-03-23 1991-12-06 Inax Corp 吐出口構造
JPH04112954U (ja) * 1991-03-20 1992-10-01 株式会社イナツクス 水栓の吐水口構造
JP2569094Y2 (ja) * 1993-02-06 1998-04-22 株式会社イナックス 断熱キャップの取付構造
JP2569095Y2 (ja) * 1993-03-17 1998-04-22 株式会社イナックス 断熱キャップの取付構造
JPH06306901A (ja) * 1993-04-22 1994-11-01 Toyoda Gosei Co Ltd 吐水口の整流板
JP5151760B2 (ja) * 2008-07-22 2013-02-27 住友金属鉱山株式会社 向流式直接加熱型熱交換器
JP5496689B2 (ja) * 2010-01-07 2014-05-21 住友重機械工業株式会社 流動床反応炉
CN204787914U (zh) * 2015-06-29 2015-11-18 广西农垦糖业集团红河制糖有限公司 一种用于汽凝水散热的恒温装置
AU2017235506B9 (en) * 2016-03-18 2019-02-14 Sumitomo Metal Mining Co., Ltd. Countercurrent-type direct-heating heat exchanger

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CU20180099A7 (es) 2019-09-04
PH12018501730A1 (en) 2019-06-17
AU2017232774B9 (en) 2019-02-14
JP6631346B2 (ja) 2020-01-15
EP3431910A4 (en) 2019-12-04
WO2017159836A1 (ja) 2017-09-21
JP2017166786A (ja) 2017-09-21
AU2017232774B2 (en) 2019-01-24
EP3431910A1 (en) 2019-01-23
AU2017232774A1 (en) 2018-08-23

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