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    • 8. 发明专利
    • Process for removing phosphate in liquid
    • 在液体中去除磷酸盐的方法
    • JPS59142894A
    • 1984-08-16
    • JP1376483
    • 1983-02-01
    • Mitsubishi Heavy Ind Ltd
    • ISHIBASHI YASUMASAKAYANO ISAMUNAKAGAWA HIRAYASUKAMIYOSHI HIDEKI
    • C02F1/58
    • PURPOSE: To remove phosphates in waste liquid effectively and to contrive to save resources and to reutilize wastes by bringing solid wastes contg. a large amt. of Ca and F compds. contained in the waste water of stack gas desulphurization process into contact with the water to be treated.
      CONSTITUTION: The water to be treated 1 is mixed and brought into contact with powdery sludge 3 and recycled seed crystals 7 in a crystallization reaction vessel 2. In this stage, the phosphates contained in the water to be treated deposit on the surface of the powdery sludge 3 and the recycled seed crystals 7 in the form of crystals of calcium phosphate. At the start of the operation, the powdery sludge is charged in a proportion to obtain 5W10g/l liq. mixture, but the amt. of the charge is set in the stationary state of the operation to obtain a weight ratio of Ca contained in said powdery sludge to the phosphate contained in the water to be treated to be 1:(3W5). The liquid mixture in the crystallization reaction vessel 2 is transferred to a precipitation vessel 5 where it is separated into water to be treated 6 and seed crystal 7 to be recycled.
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:有效去除废液中的磷酸盐,并通过固体废物来节约资源和废弃物再利用。 一个大的 的Ca和F化合物 堆放在废气中的烟气脱硫过程与待处理的水接触。 构成:将待处理的水1与结晶反应容器2中的粉状污泥3和再循环晶种7混合并与之接触。在此阶段,待处理水中所含的磷酸盐沉积在粉末状的表面上 污泥3和磷酸钙晶体形式的回收晶种7。 在操作开始时,以一定比例填充粉状污泥,得到5-10g / l liq。 混合物,但amt。 的电荷被设定为操作的静止状态,以获得所述粉末状污泥中所含的Ca与待处理水中所含的磷酸盐的重量比为1:(3-5)。 将结晶反应容器2中的液体混合物转移到沉淀容器5中,在其中分离成待处理的水6和晶种7以进行再循环。
    • 9. 发明专利
    • Process for removing phosphate in liquid
    • 在液体中去除磷酸盐的方法
    • JPS59142893A
    • 1984-08-16
    • JP1376383
    • 1983-02-01
    • Mitsubishi Heavy Ind Ltd
    • ISHIBASHI YASUMASAKAYANO ISAMUNAKAGAWA HIRAYASUKAMIYOSHI HIDEKI
    • C02F1/58
    • PURPOSE: Phosphates contained in liquid are effectively removed by bringing particulate material contg. an insoluble Ca salt into contact previously with the water to be treated, then allowing further the particulate material to contact with the water to be treated in the presence of Ca salt and be separated.
      CONSTITUTION: Phosphate-contg. water to be treated is introduced into a crystallization reaction vessel 3 while mixing with a Ca salt 2 contg. ≥ equiv. amt. of Ca. The pH of the water to be treated is adjusted to 6W8 in the crystallization reaction vessel, and the crystallization reaction proceeds by the mixing and contact of seed crystals 10 for the preliminary contact, water to be treated 1, and Ca salt 2. The liquid mixture is separated in the succeeding solid-liquid separating vessel 4 to supernatant water 5 and precipitated seed crystals 6. Most of the seed crystals 6a among the precipitated seed crystals 6 are returned continuously to the crystallization reaction vessel 3, and a part of the seed crystals are discharged as excessive seed crystal 7 out of the system intermittently or introduced continuously into a regeneration vessel as seed crystals for regeneration 6b.
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:通过引入颗粒物质来有效地除去液体中含有的磷酸盐。 不溶性Ca盐预先与待处理的水接触,然后允许颗粒物质在Ca盐存在下与待处理的水接触并分离。 组成:磷酸盐contg。 将待处理的水引入结晶反应容器3中,同时与Ca盐2混合物混合。 > =等于 AMT。 的Ca. 待结晶水的pH值在结晶反应容器中调节至6-8,结晶反应是通过与预接触的晶种10,待处理水1和Ca盐2的混合和接触进行的。 将液体混合物在随后的固液分离容器4中分离成上清液5和沉淀的晶种6.沉淀的晶种6中的大部分晶种6a连续返回到结晶反应容器3, 晶种作为过量的晶种7从系统间歇地排出或连续引入再生容器中作为用于再生的晶种6b。
    • 10. 发明专利
    • Method and apparatus for recovering soda ash
    • 用于恢复SODA ASH的方法和装置
    • JPS58202016A
    • 1983-11-25
    • JP8542582
    • 1982-05-20
    • Mitsubishi Heavy Ind Ltd
    • MATSUI KAZUOISHIBASHI YASUMASA
    • C21C5/38B01D50/00B01D51/00B01D51/04B01D51/10
    • PURPOSE: To prevent the clogging and the corrosion of a dust collection apparatus, by a method wherein a gas is sent into the dust collecting apparatus while the temp. and the moisture of the gas are regulated during a period for introducing the gas into the dust collecting apparatus and air from the outside of a furnace heated by a heat accumulator is introduced into the dust collecting apparatus during a period not introducing the gas into said dust collecting apparatus to constantly adjust the temp. in the dust collecting apparatus.
      CONSTITUTION: A dust-containing gas from an oxygen steel manufacturing furnace 1 is mainly introduced into a heat recovery device 6 and the part thereof is introduced into a heat accumulator 7 to be heated by the heat accumulating part 7b thereof. These gases are further guided to an evaporative cooling tower 10 to lower the temp. thereof to a set temp. while simultaneously humidified and soda ash and other dusts in the exhaust gas are recovered by a dry dust collecting apparatus 3. When the generation of a high temp. gas in the oxygen steel manufacturing furnace 1 is stopped, in order to prevent the lowering in the temp. of the dry dust collecting apparatus 3, an auxiliary blower 4b is operated to guide air in the vicinity of the furnace 1 to the heat accumulating part 7b and heated to a high temp. to be introduced into the dust collecting apparatus 3.
      COPYRIGHT: (C)1983,JPO&Japio
    • 目的:为了防止灰尘收集装置的堵塞和腐蚀,通过将气体送入集尘装置的方法, 在将气体引入集尘装置的期间,气体的湿度被调节,在不将气体引入所述尘埃的期间内,从由蓄热器加热的炉的外部的空气被引入集尘装置 收集装置不断调节温度。 在集尘装置中。 构成:来自氧钢制造炉1的含尘气体主要被引入热回收装置6,并将其一部分引入蓄热器7中,以被其蓄热部分7b加热。 这些气体被进一步引导到蒸发冷却塔10以降低温度。 到设定温度 同时通过干式集尘装置3回收废气中的苏打灰和其他灰尘同时加湿。 氧钢制造炉1中的气体停止,以防止温度降低。 在干燥集尘装置3中,辅助鼓风机4b被操作以将炉1附近的空气引导到蓄热部7b并被加热到高温。 被引入到集尘装置3中。