公开(公告)号：US3975247A

公开(公告)日：1976-08-17

申请号：US435655

申请日：1974-01-23

Applicant: Bernard J. Stralser

Inventor： Bernard J. Stralser

IPC: C02F1/00 ,  C02F1/461 ,  C02F1/463 ,  C02F1/465 ,  C02F1/467 ,  C02F1/72 ,  C02F3/28 ,  C02F9/00 ,  C25B1/26 ,  C02B1/82

CPC classification number: C02F1/4672 ,  C02F1/46104 ,  C02F1/001 ,  C02F1/4674 ,  C02F1/727 ,  C02F2001/46138 ,  C02F2001/46152 ,  C02F2103/005 ,  C02F2103/20 ,  C02F2103/26 ,  C02F2201/001 ,  C02F2201/4611 ,  C02F2303/04 ,  C02F3/286 ,  C02F9/00

Abstract: The waste sewage that accumulates from humans, animals and vegetables is first diluted with water to provide a product comprising twenty parts water to one part solids by weight. This diluted product is subjected to a macerating and comminuting and mixing operation that breaks down the lumps in the solids to a size where they are either dissolved or carried in suspension. From the macerator, the fluid is moved up through a screen chamber having a screen of 1/8 inch to remove any heavy, large particles therein and is next pumped into non-conductive electrolytic cell containers. An overflow connection returns any gas and excess liquid into the screening chamber. In the electrolytic cell, the fluid is passed up and down between a plurality of electrode plates of platinum-coated titanium, that are essentially unattacked by the fluid contents and do not contribute any of their metal to the reaction, which are so connected that current flows across the flow of fluid repeatedly with only one end electrode of the plurality connected to the positive side of a direct current source and the other end electrode connected to the negative side of the current source. Enough voltage is supplied to maintain a current flow of 0.25 to 1.0 amperes per square inch of electrode surface. Thus the fluid is passed repeatedly across the current path and is subjected to a continuously step-by-step changing of the level of potential with respect to the original ground voltage of the fluid entering the cell. In each passage across the current, the fluid is changed by the reactions and most of the gases evolved are removed from the field of reaction upward so as to present a newly constituted fluid to the next passage. The effluent from the cell is cleared of the solids by a skimming and filtering action to recover the water for re-use and the solids for return to earth.

Abstract translation: 首先用水稀释从人类，动物和蔬菜中积累的废污水，以提供包含20份水至1份重量份固体的产品。 将该稀释的产物进行浸渍和粉碎和混合操作，将固体中的块分解成其溶解或携带悬浮液的尺寸。 从浸渍机中，将流体向上移动通过具有1/8英寸筛网的筛分室，以除去其中重的大颗粒，然后将其泵入非导电电解池容器中。 溢出连接将任何气体和多余的液体返回到筛分室。 在电解池中，流体在镀铂的钛的多个电极板之间上下传递，其基本上不被流体内容物攻击，并且不会使它们的任何金属与反应相关联， 流过流体流动，只有一个端电极连接到直流电源的正极，而另一端电极连接到电流源的负极侧。 提供足够的电压以保持每平方英寸电极表面的电流为0.25至1.0安培。 因此，流体在电流路径上重复通过，并且相对于进入电池的流体的原始接地电压经受连续逐步地改变电位水平。 在通过电流的每个通道中，通过反应改变流体，并且大部分放出的气体向上移出反应场，以便将新构成的流体提供给下一通道。 通过撇渣和过滤作用清除细胞中的流出液，以回收再次使用的水和固体返回地球。