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    • 61. 发明公开
    • DESALTING SYSTEM AND METHOD OF DESALTING
    • ENTSALZUNGSSYSTEM UND ENTSALZUNGSVERFAHREN
    • EP2508481A4
    • 2015-09-02
    • EP10833104
    • 2010-11-16
    • MITSUBISHI HEAVY IND LTD
    • TAKEUCHI KAZUHISAITO YOSHIAKIKAKIGAMI HIDEMASAIWAHASHI HIDEOMATSUI KATSUNORITANAKA KENJI
    • C02F1/44B01D61/02B01D61/04B01D61/10B01D61/12B01D61/58C02F1/76
    • C02F1/441B01D61/025B01D61/04B01D61/10B01D61/12B01D2311/04C02F1/76C02F2209/06Y02A20/131B01D2311/2649B01D2311/12
    • A desalination apparatus includes a pretreatment device (13) having a pretreatment membrane (13a) that filters suspended matters in raw water (11) with added chlorine-containing water (12), a reverse osmosis membrane device (17) having a reverse osmosis membrane (16) that removes a salt content from filtrate water (14) supplied from the pretreatment device (13) to produce permeated water (15), and a reducing-agent injection device (30) that neutralizes the added chlorine on an upstream side of the reverse osmosis membrane device (17). The reducing-agent injection device (30) extracts a part (14a) of the filtrate water (14), adds metering SBS solution (18) to the part, obtains a maximum change point (equivalence point) of the oxidation-reduction potential of a reducing agent and chlorine, obtains reducing-agent additive concentration (Csm) corresponding to the equivalence point, and supplies the SBS solution (18) corresponding to the concentration to the filtrate water (14) to thereby neutralize the chlorine.
    • 脱盐装置包括:具有预处理膜(13a)的预处理装置(13),其利用加入的含氯水(12)对原水中的悬浮物进行过滤,反渗透膜装置(17)具有反渗透膜 (16),其从所述预处理装置(13)提供的滤液水(14)中除去盐含量,以产生渗透水(15);和还原剂注入装置(30),其中和上游侧的添加氯 反渗透膜装置(17)。 还原剂注入装置(30)提取滤液水(14)的一部分(14a),将计量SBS溶液(18)加入到该部分,获得氧化还原电位的最大变化点(当量点) 还原剂和氯,获得对应于当量点的还原剂添加剂浓度(Csm),并将与浓度相对应的SBS溶液(18)提供给滤液水(14),从而中和氯。
    • 62. 发明专利
    • جهاز وطريقة لتحلية الماء
    • SA3919B1
    • 2015-03-01
    • SA110310878
    • 2010-11-27
    • MITSUBISHI HEAVY IND LTD
    • ITO YOSHIAKITAKEUCHI KAZUHISATANAKA KENJIIWAHASHI HIDEO
    • الملخص: جهاز appratus تحليةماء desalination يتضمنجهاز device غشاء membrance تناضح osmosis عكس reverse أول 13 والذييزلمكونالملح salt منماءخام raw water يتمإمدادهبضغط pressure محددسابقاً،جهازغشاءتناضحعكسيثاني 15 والذييزيلمكونالملحفيماءمنفذ permeatedأول 12 منجهازغشاءالتناضحالعكسيالأول 13،صمام valve تنظيم regulation تدفق flow أول 17 والذييتنظممعدلتدفق flow rate الماءالمركز concentrated الأول 16 منجهازغشاءالتناضحالعكسيالأول 13،صمامتنظيمتدفقثاني 19 والذيينظممعدلتدفقالماءالمركزالثاني 18 منجهازغشاءالتناضحالعكسي 15،وجهازتحكموالذييقيسدرجةحرارة temperature إمدادالماءالخام 11 بواسطةترمومتر thermometer 20،يتحكمفيصمامتنظيمالتدفقالأول 17 للحفاظعلىكميةتصريف descharge ماءمركزثابتة،ويتحكمفيصمامتنظيمالتدفقالثاني 19 لتقليلكميةالماءالعائدةلأداءالعمليةبحيثبتمالتحكمفيمعدلتدفقإمدادجهازغشاءالتناضحالعكسيالأول 13 ليكونأقلمنمعدلالتدفقفيالصيفوالذيبهتكوندرجةالحرارةعالية،ويتمالحفاظعلىمعدلاستراداد recovery ratio محددسابقاًلمنتجالماءإلىكميةمحددةسابقاً.
    • 63. 发明专利
    • System for producing magnesium chloride aqueous solution and system for producing magnesium
    • AU2020420155A1
    • 2022-07-28
    • AU2020420155
    • 2020-12-14
    • MITSUBISHI HEAVY IND LTD
    • ITO YOSHIAKITAKEUCHI KAZUHISAKIYOSAWA MASASHI
    • C01F5/32C22B3/10C22B3/44C22B26/22C25C3/04
    • One purpose of the present invention is to provide a system for producing a magnesium chloride aqueous solution, said system making it possible to further reduce drug-related costs compared to conventional methods. The present invention relates to a system for producing a magnesium chloride aqueous solution, said system comprising: a crystallization unit that adds a sodium hydroxide aqueous solution to to-be-treated water consisting of seawater as a feedstock material, and generates a reaction slurry having magnesium hydroxide particles dispersed therein; a precipitation unit that stores the reaction slurry, and causes the precipitation of particles to separate the reaction slurry into recovered slurry and a separated liquid; a removal unit that removes divalent positive ions from the to-be-treated water or separated liquid, and generates a reaction liquid; an acid-alkali generation unit that generates a sodium hydroxide aqueous solution and hydrochloric acid from the reaction liquid; and a reaction unit that adds the hydrochloric acid to the recovered slurry, and generates a magnesium chloride aqueous solution. The acid-alkali generation unit includes: a main unit that generates the sodium hydroxide aqueous solution and the hydrochloric acid from the reaction liquid; a first connection unit that supplies the sodium hydroxide aqueous solution to the crystallization unit; and a second connection unit that supplies the hydrochloric acid to the reaction unit.
    • 65. 发明专利
    • ITMI951634A1
    • 1997-01-26
    • ITMI951634
    • 1995-07-26
    • MITSUBISHI HEAVY IND LTD
    • TAKEUCHI KAZUHISAFUJIOKA YUUICHI
    • B01D53/84C12P3/00C12S1/02F03G7/04
    • In a method of desulfurization used at a geothermal power plant, stem removed from a production well, after being used for power generation, is condensed and separated into condensed water and hydrogen sulfide-containing gas, and the hydrogen sulfide-containing gas is treated at biochemical treatment tank. The initial cell density of the reactor liquid of the biochemical treatment tanks is adjusted by cell culture liquid obtained from a cell breeding culture tank provided independently of the biochemical treatment tanks and water or a part of hot water returning to a reduction well, hydrogen sulfide-containing gas is supplied thereinto and desulfurized thereat. With lowering of activation at the biochemical treatment tanks and with lowering of desulfurization ability there, the acidified reaction liquid is removed and is added to the hot water returning to the reduction well. Accordingly, addition of inorganic nutritive salt for cell breeding becomes unnecessary. A geothermal power plant desulfurization system is constructed so that cells are separated by use of a cell separation filter from the acidified reaction liquid removed from the biochemical treatment tanks and the cells so separated are returned to the biochemical treatment tanks.