14. The apparatus of claim 13, furt

14. The apparatus of claim 13, further comprising a fermentation tank, into which the sludge which has been solubilized in the solubilizing device is introduced and subjected to a fermentation treatment, and the sludge which has been subjected to the fermentation treatment in said fermentation tank is returned to the first anaerobic tank.
15. The apparatus of claim 14, further comprising means for supplying some of the sludge which has been subjected to the fermentation treatment in the fermentation tank to the second anaerobic tank.
16. The apparatus of claim 15, further comprising means for supplying at least some of the sludge separated in said solid/liquid separating device directly to the first anaerobic tank.
17. An apparatus for the biological removal of phosphorus from raw water, the apparatus comprising: a first anaerobic tank into which the raw water and activated sludge are introduced to form a mixed liquor, an anoxic tank in which bound oxygen is applied to the mixed liquor from said first anaerobic tank, an aerobic tank in which the mixed liquor from said oxygen-free tank is aerated, mixed liquor returning means which returns some of the mixed liquor from said aerobic tank to the oxygen-free tank, first solid/liquid separating means in which the mixed liquor flowing out of said aerobic tank is subjected to solid/liquid separation, means whereby some of the solid/liquid separated sludge from said first solid/liquid separating means is returned as the activated sludge to the first anaerobic tank, a second anaerobic tank in which the remaining solid/ liquid separated sludge from the first solid/liquid separating means is maintained anaerobically and the phosphorus is released, second solid/liquid separating means in which the sludge admixed liquid from said second anaerobic tank is subjected to solid/liquid separation,solubilizing means in which the sludge separated in said second solid/liquid separating means is solubilized, solubilized sludge returning means with which at least some of the sludge which has been solubilized in said solubilizing means is returned to the first anaerobic tank, means for supplying at least some of the sludge which has been solubilized in the solubilizing means to said second anaerobic tank, and phosphorus-removing means for removing phosphorus from water which has been separated in the second solid/liquid separating means.

結果 (中文) 1:

14.该仪器索赔 13，进一步组成的发酵罐，其中污泥，已被溶解在溶解装置是介绍和进行发酵处理，并一直受到说的发酵罐的发酵处理的污泥回到第一厌氧池。15.该仪器索赔 14，进一步组成的手段，提供了一些遭受到二厌氧池发酵罐中发酵处理的污泥。16.该仪器索赔 15，进一步组成的手段供至少一些污泥分离在说固液分离设备直接向首个厌氧池。17.一种用于生物除磷从原水，组成的器具设备: 原水及活性的污泥的引入，形成混合的液，其中厌氧池绑定氧第一厌氧池应用于混合液从说第一厌氧池，曝气池混合的液从说无氧池好氧池返回第一次返回到无氧油罐，说好氧池混合液的一些手段固液混合的液分离的流出说好氧池混合的液受到固液分离手段意味着藉一些固液分离以污泥从说第一固液分离手段返回作为首个厌氧池活性污泥从第一固液分离手段剩余固 / 液分离的污泥厌氧保持和释放磷第二厌氧池，二固液分离的手段，污泥掺液体从说第二厌氧池遭受固液分离，溶的手段中，污泥中分离说，增溶二固液分离手段增溶的污泥返回意味着，至少一些污泥，已溶解在说溶手段回到第一的厌氧池，就意味着至少提供一些污泥，已被溶解在溶说第二厌氧池和磷去除水相距二固液分离手段中磷去除的手段。

結果 (中文) 3:

14。该设备的索赔13，进一步包括一个发酵罐，使污泥已溶解在溶解装置的介绍，进行发酵处理，而污泥已遭受在发酵罐是回到第一厌氧池发酵处理。
15。索赔的装置14，还包括用于在发酵罐中发酵处理的污泥中的一些装置。该设备的索赔15，进一步包括用于供应至少一些在所述固体/液体分离装置中分离的污泥直接到第一厌氧罐。一种生物脱氮除磷装置，其包括：将原水和活性污泥引入到该混合液中，在所述第一厌氧池、所述氧气罐中所述混合液从所述氧气罐中的混合液中施加一个缺氧池，混合液返混，从所说的好氧池中返回一些混合液，先固/液分离装置在所述好氧池内的混合液进行固液分离，所以一些固/液分离污泥从所述第一固/液分离装置是为活性污泥厌氧池返回的第一，第二厌氧池中剩余的固体/液体分离污泥从第一固/液分离手段维持厌氧磷释放，二固/液分离装置，污泥混合液从所述第二厌氧池进行固液分离，溶解指污泥分离的第二固/液分离装置溶解，溶解污泥回流的方式，至少部分的污泥已溶解在溶解的意思是说回到第一厌氧池，提供至少部分的污泥已溶解在溶解意味着第二厌氧池说，二次固液分离装置中分离出的磷的去除方法。