公开(公告)号：US20020189987A1

公开(公告)日：2002-12-19

申请号：US10168130

申请日：2002-06-19

Inventor： Patrick Wagner

IPC: B01D035/02

CPC classification number: B63J1/00 ,  B01D61/025 ,  B01D61/10 ,  B01D61/12 ,  C02F1/441 ,  C02F2201/001 ,  Y02A20/131

Abstract: The invention concerns a seawater desalination system comprising a reverse osmosis cell (12) containing a semi-permeable membrane for performing desalination of the water by passing seawater under pressure through the membrane, a pump (20) for forcing the pressurized seawater through said membrane and a mechanism driving the pump shaft comprising a direct current motor (22) and an alternating current motor (24), the two motors being mounted in position for driving the pump shaft with a belt, and also comprising clutch means for preventing one of the motors from being driven in rotation while the other motor is activated and drives the pump shaft in rotation.

Abstract translation: 本发明涉及一种海水淡化系统，其包括反渗透池（12），该反渗透池包含用于通过在压力下通过海水使海水脱盐的半透膜，用于迫使加压海水通过所述膜的泵（20） 驱动泵轴的机构包括直流电动机（22）和交流电动机（24），所述两个电动机安装在适当位置以便用带驱动泵轴，并且还包括用于防止一个电动机 在另一个电动机被启动并驱动泵轴旋转时被驱动旋转。

公开(公告)号：US06207047B1

公开(公告)日：2001-03-27

申请号：US09272799

申请日：1999-03-19

Applicant: Richard Gothreaux

Inventor： Richard Gothreaux

IPC: C02F306

CPC classification number: C02F3/06 ,  C02F1/505 ,  C02F2201/001 ,  Y02W10/15

Abstract: A device for the treatment of wastewater is provided. The basic device includes a wastewater inlet, a connecting means and a bioreactor. The bioreactor is a substantially water-tight compartment which has its bioreactor inlet fluidly connected to the connecting means which is fluidly connected to the wastewater inlet. Inside the substantially water-tight compartment is controlled porous media inoculated with nitrifying aerobic bacteria. Additionally, many applications will require a plurality of bioreactors to be able to handle larger loads of wastewater. The plurality of bioreactors are connected in series by a plurality of bioreactor connecting means, each bioreactor connecting means fluidly connecting one bioreactor's outlet to another bioreactor's inlet. Effluent enters the plurality of bioreactors through first bioreactor's inlet and exits the plurality of bioreactors from the last bioreactor's outlet. In order to handle the greatest amount of wastewater, the plurality of bioreactors is connected to a primary treatment tank and a biofiltration tank. A primary pump directs effluent from the primary treatment tank to the biofiltration tank. The primary pump is activated when the volume in the primary treatment tank reaches an activation capacity and is deactivated when the volume in the primary treatment tank reaches a deactivation capacity. The biofiltration tank contains controlled porous media inoculated with nitrifying aerobic bacteria. A secondary pump directs effluent from the biofiltration tank to the first bioreactor's inlet.

Abstract translation: 提供了一种处理废水的设备。 基本装置包括废水入口，连接装置和生物反应器。 生物反应器是基本上不透水的室，其生物反应器入口流体地连接到流体连接到废水入口的连接装置。 在基本不透水的隔室内部是用硝化好氧细菌接种的受控多孔介质。 此外，许多应用将需要多个生物反应器能够处理较大负荷的废水。 多个生物反应器通过多个生物反应器连接装置串联连接，每个生物反应器连接装置将一个生物反应器的出口流体连接到另一生物反应器的入口。 流出物通过第一生物反应器的入口进入多个生物反应器并从最后的生物反应器的出口离开多个生物反应器。 为了处理最大量的废水，多个生物反应器连接到初级处理槽和生物滤池。 初级泵将污水从初级处理槽引导到生物滤池。 当主处理槽中的体积达到活化能力时，主泵被激活，并且当主处理槽中的体积达到钝化能力时，初级泵被激活。 生物过滤罐包含用硝化好氧细菌接种的受控多孔介质。 次级泵将流出物从生物过滤罐引导到第一生物反应器的入口。

公开(公告)号：US4292175A

公开(公告)日：1981-09-29

申请号：US63581

申请日：1979-08-03

Applicant: William A. Krause ,  Leonard E. Langeland

Inventor： William A. Krause ,  Leonard E. Langeland

IPC: C02F1/467 ,  C02F9/00 ,  C02F1/46 ,  C02F1/76

CPC classification number: C02F1/4674 ,  C02F2103/002 ,  C02F2103/005 ,  C02F2201/001

Abstract: A compact, relatively small unit for treatment of wastewater for discharge into maritime waters is disclosed. The wastewater is received in a surge or retention tank and is delivered by gravity flow or pumped to a macerator for comminution of the solids content of the wastewater. Prior to entering the macerator, salt water on a controlled flow basis is added to the wastewater in sufficient amounts to insure a high enough salt content for use as the electrolyte in an electrocatalytic cell. From the macerator the wastewater to be treated is directed into a vertically oriented, elongated, electrocatalytic cell having a plurality of parallel, closely spaced electrodes therein positioned parallel to the flow of wastewater therethrough. The wastewater is directed through the electrocatalytic unit. The end electrodes of the spaced electrode plates are connected to a source of direct current sufficient to generate chlorine, oxygen and other treating chemicals in situ. The gases generated in the cell, entrained with the liquid, flow out of the electrocatalytic cell with the liquid into the standpipe of an effluent tank where a negative pressure separates the entrained gases from the liquid and vents them to the atmosphere. The heavier solids remaining in the discharged treated liquid are allowed to settle in the bottom of the effluent tank and the remaining effluent is discharged.

Abstract translation: 公开了用于处理排放到海水中的废水的紧凑的，相对较小的单元。 废水被接收在浪涌或保留槽中，并通过重力流输送或泵送到浸取器以粉碎废水的固体含量。 在进入剥离器之前，将以受控流动为基础的盐水以足够的量添加到废水中，以确保足够高的盐含量用作电催化池中的电解质。 从浸渍机将待处理的废水引导到垂直取向的细长的电催化池中，其具有多个平行的，紧密间隔的电极，其平行于废水流通过。 废水被引导通过电催化装置。 间隔开的电极板的端电极连接到足以产生氯气，氧气和其他处理化学品的直流电源。 在液体中携带的气体中产生的气体与液体一起从电催化池流出到排出罐的立管中，其中负压将夹带的气体与液体分离并排放到大气中。 排出的处理液体中残留的较重的固体被允许沉淀在流出槽的底部，并排出剩余的流出物。

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。

公开(公告)号：US3898161A

公开(公告)日：1975-08-05

申请号：US39683973

申请日：1973-09-13

Applicant: STANDARD PRODUCTS CO

Inventor： REID JAMES S

IPC: B01D3/08 ,  C02F1/04 ,  C02F3/00 ,  C02F9/00 ,  B01D43/00 ,  B01D15/00

CPC classification number: C02F3/006 ,  B01D3/08 ,  C02F1/048 ,  C02F2103/005 ,  C02F2201/001

Abstract: A waste disposal system includes vaporizing means for vaporizing liquid and organic human bacteriological waste material. Ash and other materials are periodically flushed from the vaporizing means by a fresh water flushing arrangement.

Abstract translation: 废物处理系统包括蒸发液体和有机人体细菌废料的蒸发装置。 灰分和其他材料通过淡水冲洗装置从蒸发装置周期性地冲洗。

公开(公告)号：US3846301A

公开(公告)日：1974-11-05

申请号：US27825172

申请日：1972-08-07

Applicant: SANITAS CO LTD

Inventor： STOKES J ,  COUSINS A

IPC: C02F1/50 ,  B03B9/06 ,  C02F1/467 ,  C02F1/66 ,  C02F1/72 ,  C02F9/00 ,  C02B1/36

CPC classification number: B03B9/06 ,  C02F1/4674 ,  C02F1/66 ,  C02F2103/005 ,  C02F2201/001 ,  Y10S210/916

Abstract: 1. A METHOD OF TREATING SEWAGE COMPRISING THE STEPS OF: (A) FLUSHING SEWAGE FROM A PLURALITY OF RECEIVERS BY MEANS OF FLUSHING LIQUID, THUS FORMING A MIXTURE OF (B) SEPARATING THE MIXTURE INTO A FIRST PART WHICH HAS (B) SEPARATING THE MIXTURE INTO A FIRST PART WHICH HAS A HIGH CONTENT OF SOLID MATTER AND A LOW CONTENT OF LIQUID AND INTO A SECOND PART WHICH HAS A HIGH CONTENT OF LIQUID, (C) AFTER STEP (B) SEPARATING, AT A SUPERATION ZONE, SAID SECOND PART INTO A SOLID MATTER PORTION AND A LIQUID PORTION, (D) MAINTAINING A CAUSTIC ALKALI CHEMICAL COMPOSITION IN SAID LIQUID PORTION AT A CONCENTRATION NOT EXCEEDING ONE PERCENT SUCH THAT SAID LIQUID PORTION IS DISINFECTANT AND DEODORANT, (E) MAINTAINING A BLEACHING ACTION IN SAID LIQUID PORTION SO AS TO HAVE A DECOLORISING EFFECT, (F) USING SAID LIQUID PORTION AS SAID FLUSHING LIQUID FOR REPETITION OF STEP (A), (G) AFTER STEP (B) CONVEYING THE FIRST PART AWAY FROM SAID SEPARATION ZONE TO A COMMINUTION ZONE REMOTE FROM SAID SEPARATION ZONE AND SUBJECTING SAID FIRST PART TO MECHANICAL REDUCTION OF THE SIZE OF THE PIECES OF THE SOLID MATTER THEREOF, (H) PROVIDING A STORAGE ZONE REMOTE FROM SAID SEPARATION ZONE FOR STORAGE OF THE SOLID MATTER; (I) AFTER STEP (G), CONVEYING THE FIRST PART HIGH IN SOLID CONTENT FROM SAID COMMINUTING ZONE TO SAID STORAGE ZONE WHEREBY SUBSTANTIALLY ALL OF THE SOLID MATTER OF SAID FIRST PART IS SUBJECTED TO THE CHEMICAL CONTENT OF THE LIQUID CONTENT THEREOF AND IS THEREBY BROKEN DOWN, DISPERSED, STERILISED AND DEODORISED; AND (J) TRANSFERRING SAID SOLID MATTER PORTION SEPARATED FROM SAID SECOND PART TO SAID STORAGE ZONE.

公开(公告)号：US3807564A

公开(公告)日：1974-04-30

申请号：US31245872

申请日：1972-12-06

Applicant: HESS H ,  COLE E

Inventor： COLE E ,  HESS H

IPC: C02F1/02 ,  C02F9/00 ,  C02F11/08 ,  C10B53/00 ,  B01D17/00

CPC classification number: C10B53/00 ,  C02F1/025 ,  C02F11/08 ,  C02F2201/001

Abstract: A compact sewage treatment unit has at least one pressure vessel containing a heat exchanger in which a waste stream is heated to coking temperature to coke the bulk of the organic wastes except for greases which are collected in a trap tray in the upper part of the heat exchanger and discharged. Gas formed during coking is removed through a pressure relief valve. A trap tray near the bottom of the heat exchanger serves to separate the coke and the decoked effluent. The effluent passes around the tube and up the side of the pressure vessel to serve as a heat transfer medium for the coking reaction and for heating the incoming waste slurry to coking temperature. A sparger is provided above the heated zone for bringing oxygen or air in contact with the decoked effluent to oxidize any dissolved organic materials which were not coked. The unit is particularly useful for shipboard use and in apartments.

公开(公告)号：US3788476A

公开(公告)日：1974-01-29

申请号：US3788476D

申请日：1971-09-23

Applicant: OTHMER D

Inventor： OTHMER D

IPC: C02F1/72 ,  C02F3/12 ,  C02F9/00 ,  C02F11/08 ,  B01D21/06 ,  B01D21/24

CPC classification number: C02F3/1242 ,  C02F1/72 ,  C02F11/08 ,  C02F2201/001 ,  C02F2301/066 ,  Y02W10/15 ,  Y02W10/30

Abstract: A system is described for removing pollutants of waste waters, including domestic and other sewage, by simultaneous oxidation of organic wastes, both soluble and insoluble, and by sedimentation of insoluble particles causing turbidity. This is essentially a conventional solids-liquid contactor clarifier with some additions to provide means for: (a) addition of air or purer oxygen to sewage waters; (b) pressurizing the sewage water up to 10 atmospheres to increase solubility and concentration of oxygen-hence velocity of chemical and/or aerobic reaction; (c) withdrawing and depressurizing the sewage water to atmospheric pressure to allow most of dissolved gases to be released and to be discharged because of lower solubility for gases at atmospheric pressure; (d) recycling the sewage water for from 2 to 50 times through this pressurizing-depressurizing cycle; and, when used aboard ship, (e) means for installation in the ship''s hold to minimize effects of the ship''s movements on the sedimentation operation. It is particularly useful for smaller installations, for use on ships, and other places where waste from not more than several thousand people is to be handled. It also may be used as a sedimentation system alone wherein insoluble solids are settled out to give a clear effluent. The sludge solids produced in an earlier sedimentation, either with or without oxidation, may be oxidized and sedimented in a separate step in the equipment.

Abstract translation: 描述了通过同时氧化可溶性和不溶性的有机废物以及引起浊度的不溶性颗粒的沉淀来描述用于去除包括家用和其他污水在内的废水污染物的系统。 这基本上是一种常规的固体 - 液体接触器澄清器，具有一些添加物，以提供用于：（a）向污水中添加空气或更纯净的氧气的装置; （b）将污水加压至10个大气压，以提高氧气的溶解度和浓度，从而提高化学和/或需氧反应的速度; （c）将污水排出和减压至大气压，以便大部分溶解气体由于在大气压下对气体的溶解度较低而释放并排放; （d）通过该加压 - 减压循环将污水循环2至50次; 并在船上使用时，（e）安装在船舶上的装置，以尽量减少船舶运动对沉淀作业的影响。 对于较小的安装，用于船舶和其他不超过数千人的垃圾处理的地方特别有用。 它也可以用作单独的沉降系统，其中不溶性固体沉淀出来以产生澄清的流出物。 在较早的沉淀中产生的污泥固体，无论是否具有氧化，可能会在设备的单独步骤中被氧化和沉淀。

公开(公告)号：US3782550A

公开(公告)日：1974-01-01

申请号：US3782550D

申请日：1971-11-05

Applicant: DAYTON MFG CO

Inventor： MATERESE V

IPC: C02F9/00 ,  E03D9/10 ,  C02C1/40

CPC classification number: E03D9/10 ,  C02F2103/005 ,  C02F2201/001

Abstract: A waste treatment system which receives liquid and solid waste, macerates the solids to form a slurry and pumps the slurry to a treatment tank. In the treatment tank the solids are separated from the liquids and retained in the tank, while the liquid effluent is treated chemically to render it pathogenically harmless and discharged from the system.

Abstract translation: 接收液体和固体废物的废物处理系统，将固体浸渍以形成浆料并将浆料泵送到处理罐。 在处理槽中，固体与液体分离并保留在罐中，而液体流出物被化学处理，使其病原性无害，并从系统中排出。

公开(公告)号：US3770624A

公开(公告)日：1973-11-06

申请号：US3770624D

申请日：1970-12-14

Applicant: ECODYNE CORP

Inventor： MC KIBBEN J ,  GOODMAN B ,  HIGGINS R

IPC: C02F3/12 ,  C02F9/00 ,  C02C1/12

CPC classification number: C02F3/1242 ,  C02F2103/005 ,  C02F2201/001 ,  Y02W10/15

Abstract: THE INVENTION PROVIDES AN IMPROVED METHOD AND APPARATUS FOR TREATING WATER CONTAINING SUSPENDED SOLIDS FROM A SANITARY SYSTEM. IN CARRYING OUT THE METHOD, THE WATER IS AERATED AND DELIVERED TO A SCREEN WITH A DIRECTIONAL COMPONENT ACROSS THE SCREEN SURFACE AND A DIRECTIONAL COMPONENT THROUGH THE SCREEN. THE SCREEN HAS OPENINGS LARGE ENOUGH TO PASS THE MAJORITY OF THE SOLIDS SUSPENDED IN THE WATER, AND HAS THE ABILITY TO HOLD A COATING OF THESE SOLIDS ON ITS UPSTREAM SIDE. THE FLOW OF WATER IS CONTROLLED SO THAT A COATING OF THE SUSPENDED SOLIDS FROM THE WATER IS FORMED ON THE SCREEN SURFACE. THE DELIVERY OF WATER CONTAINING THESE SUSPENDED SOLIDS TO THE SCREEN IS CONTINUED WITH A DIRECTIONAL COMPONENT ACROSS THE SCREEN AND A DIRECTIONAL COMPONENT THROUGH THE SCREEN, WHEREBY TO FILTER SOLIDS FROM THE WATER PASSING THROUGH THE COATING AND SCREEN. THE RELATIONSHIP BETWEEN THE DIRECTIONAL COMPONENTS ACROSS AND THROUGH THE SCREEN IS CONTROLLED TO MAINTAIN THE COATING ON THE SCREEN. THE WATER THAT IS PASSED THROUGH THE SCREEN IS STORED, AND IS RECYCLED TO THE SANITARY SYSTEM.