JPS583877B2 - Consolidation relaxation method for powdered ore slurry - Google Patents

Consolidation relaxation method for powdered ore slurry

Info

Publication number
JPS583877B2
JPS583877B2 JP2169977A JP2169977A JPS583877B2 JP S583877 B2 JPS583877 B2 JP S583877B2 JP 2169977 A JP2169977 A JP 2169977A JP 2169977 A JP2169977 A JP 2169977A JP S583877 B2 JPS583877 B2 JP S583877B2
Authority
JP
Japan
Prior art keywords
ore slurry
powdered ore
consolidation
dilute acid
hold
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.)
Expired
Application number
JP2169977A
Other languages
Japanese (ja)
Other versions
JPS53107086A (en
Inventor
原田幸男
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.)
Hitachi Zosen Corp
Original Assignee
Hitachi Zosen Corp
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 Hitachi Zosen Corp filed Critical Hitachi Zosen Corp
Priority to JP2169977A priority Critical patent/JPS583877B2/en
Publication of JPS53107086A publication Critical patent/JPS53107086A/en
Publication of JPS583877B2 publication Critical patent/JPS583877B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Description

【発明の詳細な説明】 本発明は粉鉱スラリーの圧密緩和法に関するものである
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for deconsolidating fine ore slurry.

粉鉱石粉末は、積地においてスラリー状で船倉内に積載
されるが、積載後の停泊中および航海中に、水との比重
差によって沈降し、脱水された圧密状態で堆積される。
Fine ore powder is loaded into the ship's hold in the form of a slurry at the loading port, but during anchorage and voyage after loading, it settles due to the difference in specific gravity with water, and is deposited in a dehydrated, consolidated state.

このような圧密堆積状態の鉄鉱石粉末は固く、したがつ
てクラブパケットによる揚荷は容易に行なえない。
Iron ore powder in such a consolidated pile is hard and therefore cannot be easily unloaded by club packets.

このことから最近では、鉄鉱石粉末に対して上部または
下部から高圧液体を噴射し、再スラリー化をはかりなが
らポンプ輸送システムにより揚荷する方法が採られてい
る。
For this reason, a method has recently been adopted in which iron ore powder is injected with high-pressure liquid from above or below, and is unloaded using a pump transportation system while reslurrying the powder.

これによると、成程、再スラリー化により揚荷を行なう
ことができるが、前述したように圧密状態であることか
ら、高圧液体の噴射による切り崩しは、高圧のものを使
用したとしても迅速に行なえない。
According to this, it is possible to lift the cargo by re-slurrying, but as mentioned above, it is in a consolidated state, so cutting down by jetting high-pressure liquid cannot be done quickly even if high-pressure liquid is used. do not have.

これを解決するために、船倉から(圧密)粉鉱スラリー
を揚荷する前に船倉内底部から空気を挿入して圧密を緩
和させる方法が考えられている。
In order to solve this problem, a method has been considered in which air is introduced from the bottom of the hold to relieve the consolidation before unloading the (consolidated) powdered ore slurry from the hold.

しかしこの方法によると、・空気泡を送入する段階で微
細気泡を作ることは非常に困難で、ある程度大きい気泡
になる。
However, according to this method, it is very difficult to create fine bubbles at the stage of introducing air bubbles, and the bubbles end up being rather large.

・この気泡は、粉鉱スラリーの層内では合体してより大
きい気泡となる。
- These bubbles coalesce into larger bubbles within the layer of fine ore slurry.

・この気泡は層内で保持されず、上昇してしまう割合が
大きい。
・These air bubbles are not retained within the layer and tend to rise.

などの問題点がある。There are problems such as:

そこで本発明では上記問題点を解決し得る粉鉱スラリー
の圧密緩和法を提供するもので、以下その一実施例を図
面に基づいて説明する。
Therefore, the present invention provides a method for deconsolidating powdered ore slurry that can solve the above-mentioned problems, and one embodiment of the method will be described below with reference to the drawings.

1は隔壁2と底壁(二重底)3とにより形成される船倉
で、その上端にハツチ4を有すると共に底壁3にウエル
5が形成される。
Reference numeral 1 designates a hold formed by a bulkhead 2 and a bottom wall (double bottom) 3, which has a hatch 4 at its upper end and a well 5 formed in the bottom wall 3.

このウエル5には、ポンプ6を有する液体供給管7が接
続する高圧液体噴射ノズル8が設けられると共に、ポン
プ9を有する粉鉱スラリー排出管10が設けられる。
This well 5 is provided with a high-pressure liquid injection nozzle 8 to which a liquid supply pipe 7 with a pump 6 is connected, and a fine ore slurry discharge pipe 10 with a pump 9 is provided.

11は船倉1内底部に水平方向に複数設けられた希酸分
配管で、これら希酸分配管11は夫々多数の噴出孔12
を有すると共に、希酸供給管13に連通ずる。
Reference numeral 11 denotes a plurality of dilute acid distribution pipes provided horizontally at the bottom of the hold 1, and each of these dilute acid distribution pipes 11 has a large number of ejection holes 12.
and communicates with the dilute acid supply pipe 13.

第2図に示すように、船倉1内に粉鉱スラリー14を積
荷し、そして上澄水を排出した状態で揚地へと航行する
As shown in FIG. 2, the cargo hold 1 is loaded with powdered ore slurry 14, and the vessel sails to the unloading port with the supernatant water discharged.

そして揚地におけて船倉1から粉鉱スラリ−14を揚荷
する前に、希酸供給管13および希酸分配管11を介し
て各噴出孔12から希酸を噴出させる。
Before unloading the fine ore slurry 14 from the hold 1 at the unloading port, dilute acid is jetted out from each jetting hole 12 via the dilute acid supply pipe 13 and the dilute acid distribution pipe 11.

これにより希酸と粉鉱スラリー〔鉄(Fe))との反応
で水素ガス(H2)を発生させる。
As a result, hydrogen gas (H2) is generated by the reaction between the dilute acid and the powdered ore slurry (iron (Fe)).

すなわちその反応例を示すと、塩酸(HCI)の場合 Fe + 2 HCI−+FeC l 2+H2硫酸(
H2 SO4 )の場合 F e + H2 SO4→Fe SO4+H2硝酸(
HNO3)の場合 F e + 2 HNO 3→F e ( NO 3
) 2 + H2などである。
That is, to show an example of the reaction, in the case of hydrochloric acid (HCI), Fe + 2 HCI- + FeCl 2 + H2 sulfuric acid (
In the case of H2 SO4 ), Fe + H2 SO4 → Fe SO4 + H2 nitric acid (
In the case of HNO3), Fe + 2 HNO 3 → Fe ( NO 3
) 2 + H2, etc.

なお、希酸としての濃度は0.1規定濃度以下(大略0
. 0 01〜0.1規定が望ぽしい。
In addition, the concentration as a dilute acid is 0.1 normal concentration or less (approximately 0
.. A regulation of 0.01 to 0.1 is desirable.

)で送入し、粉鉱スラリー14中の水で希釈されて最終
濃度が1×10−5〜1×10−8規定程度になるのが
望ましい。
) and diluted with water in the fine ore slurry 14 to have a final concentration of about 1×10 −5 to 1×10 −8 normal.

前述した水素ガス(H2)は鉄鉱石表面で極めて微細な
気泡として発生するので気液固界面張力によって表面に
付着したままで他の気泡との合体が進行せず、層内に保
持されたままとなり層の空隙比が犬となり、圧密が緩和
される。
The aforementioned hydrogen gas (H2) is generated as extremely fine bubbles on the iron ore surface, so it remains attached to the surface due to the gas-liquid solid interfacial tension and does not coalesce with other bubbles, remaining within the layer. The void ratio of the adjacent layer becomes dog, and consolidation is alleviated.

このように圧密が緩和された粉鉱スラリー14の揚荷は
第3図に示すように、高圧液体噴射ノズル8からの高圧
液体により切り崩して再スラリー化し、そして粉鉱スラ
リー排出管10を介して行なわれる。
As shown in FIG. 3, the unloaded fine ore slurry 14 that has been deconsolidated is broken down by high-pressure liquid from the high-pressure liquid injection nozzle 8 to form a reslurry, and then passed through the fine ore slurry discharge pipe 10. It is done.

以上、実施例で述べた本発明によると、粉鉱スラリーを
揚荷する前に希酸を供給して、この希酸と粉鉱スラリー
との反応で水素ガスを発生させることから、この水素ガ
スは、鉄鉱石(粉鉱)表面で極めて微細な気泡として発
生することになって気液固界面張力によって表面に付着
し且つ他の気泡との合体が進行せずに層内に保持された
ままとなり、層の空隙比が大となって圧密が緩和される
According to the present invention described in the examples above, dilute acid is supplied before unloading the fine ore slurry, and hydrogen gas is generated by the reaction between the dilute acid and the fine ore slurry. The bubbles are generated as extremely fine bubbles on the surface of iron ore (fine ore), and they adhere to the surface due to gas-liquid solid interfacial tension and are retained within the layer without proceeding to coalesce with other bubbles. As a result, the void ratio of the layer increases and the consolidation is relaxed.

したがって再スラリー化の揚荷、すなわち高圧液体の噴
射による切り崩しは、低圧のものを使用したとしても容
易に迅速に行なうことができる。
Therefore, lifting for reslurry, ie, cutting down by jetting high-pressure liquid, can be easily and quickly performed even if a low-pressure liquid is used.

【図面の簡単な説明】[Brief explanation of drawings]

図面は本発明の一実施例を示し、第1図は横断斜視図、
第2図、第3図は作業状態を示す横断面図である。 1・・・・・・船倉、2・・・・・・隔壁、3・・・・
・・底壁、5・・・・・・ウェル、7・・・・・・液体
供給管、8・・・・・・高圧液体噴射ノズル、10・・
・・・・粉鉱スラリー排出管、11・・・・・・希酸分
配管、12・・・・・・噴出孔、13・・・・・・希酸
供給管、14・・・・・・粉鉱スラリー。
The drawings show one embodiment of the present invention, and FIG. 1 is a cross-sectional perspective view;
FIGS. 2 and 3 are cross-sectional views showing working conditions. 1... hold, 2... bulkhead, 3...
... Bottom wall, 5 ... Well, 7 ... Liquid supply pipe, 8 ... High pressure liquid injection nozzle, 10 ...
...Powdered ore slurry discharge pipe, 11...Dilute acid distribution pipe, 12...Blowout hole, 13...Dilute acid supply pipe, 14...・Powdered ore slurry.

Claims (1)

【特許請求の範囲】[Claims] 1 船倉から粉鉱スラリーを揚荷する前に船倉内底部か
ら希酸を供給し、この希酸と粉鉱スラリーとの反応で水
素ガスを発生させることを特徴とする粉鉱スラリーの圧
密緩和法。
1. A method for deconsolidating powdered ore slurry, which is characterized by supplying dilute acid from the bottom of the hold before unloading the powdered ore slurry from the ship's hold, and generating hydrogen gas through the reaction between this dilute acid and the powdered ore slurry. .
JP2169977A 1977-02-28 1977-02-28 Consolidation relaxation method for powdered ore slurry Expired JPS583877B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2169977A JPS583877B2 (en) 1977-02-28 1977-02-28 Consolidation relaxation method for powdered ore slurry

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2169977A JPS583877B2 (en) 1977-02-28 1977-02-28 Consolidation relaxation method for powdered ore slurry

Publications (2)

Publication Number Publication Date
JPS53107086A JPS53107086A (en) 1978-09-18
JPS583877B2 true JPS583877B2 (en) 1983-01-24

Family

ID=12062306

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2169977A Expired JPS583877B2 (en) 1977-02-28 1977-02-28 Consolidation relaxation method for powdered ore slurry

Country Status (1)

Country Link
JP (1) JPS583877B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3574530B2 (en) * 1996-05-13 2004-10-06 ペンタックス株式会社 Endoscope treatment tool guide

Also Published As

Publication number Publication date
JPS53107086A (en) 1978-09-18

Similar Documents

Publication Publication Date Title
US3762773A (en) Method and apparatus for feeding finely divided solids to a pressurized gas or gasliquid solids system
CN204775829U (en) A protect apart from roof beam for container ship transverse bulkhead carries on fast
KR100940795B1 (en) Method for launching and transporting heavy weight structures using air bags
JPS583877B2 (en) Consolidation relaxation method for powdered ore slurry
JP5557917B2 (en) How to prepare a dry bulk carrier
JP2002533264A (en) Loading and unloading of solid substances with high moisture content
JPS582136B2 (en) Method for preventing clogging in consolidated cargo reslurry equipment
JP2519094B2 (en) Flow reactor for trichlorosilane production
JPH0218479B2 (en)
KR101384713B1 (en) Particle transfer system
JP6597919B2 (en) Pressurized steam aging device
JPH08310482A (en) Substitute gas feeding part structure of storage tank in transport ship
CN107323619A (en) A kind of extra large land conveyer method of Large-diameter Steel cylinder
JPS5819510B2 (en) Slurry discharge port in slurry ship
US4089284A (en) Slurry vessel with dewatering ports covering more than two percent of hold bottom
JP2020056270A (en) Liquefaction countermeasure method
CN110271645B (en) Offshore crude oil lightering method
US10837152B2 (en) Methods and system for forming reclamation structures
JPS5827158B2 (en) Consolidation relaxation method for powdered ore slurry
JPS584672B2 (en) Re-slurry unloading method of fine ore
JP2589629B2 (en) Installation method of caisson by work boat
CN201473925U (en) Capacity enlarging modification device of wharf mooring capacity
JPS59167393A (en) Method of renovating hull parts around tank in low temperature liquefied gas carrying ship
JPS5822397B2 (en) Consolidated cargo reslurry equipment
JPH07121332B2 (en) Device for reducing entrainment of foreign matter in hydrogen flow