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    • 3. 发明专利
    • EXTRACTION METHOD
    • JP2000176438A
    • 2000-06-27
    • JP36108898
    • 1998-12-18
    • ELECTRIC POWER DEV COKANSAI ELECTRIC POWER COKURITA WATER IND LTD
    • NOGUCHI YOSHIKAZUMUTO KENICHITOYAMA KOJIYAMASHITA NAOYUKIASADA HIROYUKIETO YOSHIHIRO
    • C02F1/26B01D11/04
    • PROBLEM TO BE SOLVED: To stably and effectively perform a series of treatments from extraction to crystallizing recovery in by response to a variation in object concentration in water to be treated by adjusting a pH value of stripping agent before stripping based on a pH value after stripping. SOLUTION: A pipeline for feeding stripping agent in which boron has been back extracted in a stripping 3 to a crystallizer 4 is provided with a pH meter 4A to measure pH. And pH of the stripping agent before backward extraction is determined so that pH of stripping agent after backward extraction becomes a predetermined pH value. Based on this result, the operation of a chemical injection pump P2 is controlled. When pH of the stripping agent after stripping for adjusting the added quantity of alkali to a pH adjusting tank 2 is lower than a predetermined pH value, the fed quantity of alkali to the pH adjusting tank 2 is increased so that pH of the stripping agent is raised, and on the contrary, when pH of the stripping agent after backward extraction is higher than the predetermined pH value, the fed quantity of alkali to the pH adjusting tank 2 is reduced so that pH of the stripping agent is lowered. In this way, by increasing or decreasing the fed quantity of alkali, pH of the stripping agent before stripping is adjusted.
    • 8. 发明专利
    • EXTRACTION METHOD
    • JPH11653A
    • 1999-01-06
    • JP15666597
    • 1997-06-13
    • ELECTRIC POWER DEV COKURITA WATER IND LTDKANSAI ELECTRIC POWER CO
    • YAMASHITA NAOYUKITOYAMA KOJISHIRAKATA TADASHIMUTO KENICHIASADA HIROYUKIYAMADA RYOICHIHORII SHIGEKIETO YOSHIHIRO
    • C02F1/26C02F5/00
    • PROBLEM TO BE SOLVED: To prevent scale hindrance from occurring and enhance stability and efficiency by adding a same kind of or a different kind of an extractant to an extractant from which back extraction of an object substance has been carried out and separating the added extractant before the extractant is returned to an extraction part. SOLUTION: An extractant from which an object substance has been extracted is fed from an extraction tank 1 to a back extraction tank 2 comprising a mixer part and a settler part through a pipe 14 in order to carry out back extraction. A back extractant which has been subjected to back extraction is transferred to a precipitation tank 3 and an object substance is precipitated and taken out from a pipe 17. The back extractant after precipitation is returned to the back extraction tank 2 via a back extractant storage tank 5 and pipes 18, 15. A same kind of or a different kind of a second back extractant is added to the extractant which has been treated in the back extractant tank 2 via a pipe 19 and sent to an agitation/separation tank 4 and residual object substances are separated. The extractant after treatment is returned to the extraction tank 1 through a pipe 12 and the second back extractant after treatment is transferred to the back extractant storage tank 5 through a pipe 22 for use or is discharged through a pipe 23. By this method, production of scale is avoided even if operation is continued for about 300 hours.