Abstract:
The method and mechanism for desalinating seawater and brackish water in which saline water is divided into inside and outside streams. The inside stream is moved through the inside of a transport membrane. The outside stream moves across the outside of the membrane. Ions cross the membrane from one stream to another and more ions are moved from the inside stream to the outside stream than are moved from the outside stream to the inside stream. The process is powered by an Na,K-pump in which Na +   ions are moved from the inside stream to the outside stream and K +   ions move in the opposite direction. After the inside stream leaves the transport membrane, the K +   ions are replaced by Na +   ions by a suitable ion exchanger.

Description:
BACKGROUND 
     The present invention relates to desalination of seawater and brackish water and more particularly to an improved method and means of desalinating seawater and brackish water which utilizes an enzyme assisted membrane. 
     Water usage has been increasing yearly so that the demand for fresh water for municipal, industrial, and agricultural use has been growing. In some areas lower than normal rainfall has forced authorities to place restrictions on water consumption. Because of an abundance of salt water, researchers have been studying various possibilities of obtaining fresh water from salt water. Various methods of desalination of water have been used over the years. However, none of these methods appear to be satisfactory. 
     BRIEF DESCRIPTION 
     The present invention has for one of its objects an improved desalination method which uses a transport membrane to achieve excellent results. 
     Another object of the present invention is the provision of an improved desalination method in which the transport of ions across the membrane is sufficient for the replacement of more ions in one direction than in the other direction. 
     Another object of the present invention is the provision of an improved desalination method in which a transport membrane is used to permit more ions to be moved in one direction than in the other direction. 
     Another object of the present invention is the provision of an improved desalination method in which a transport membrane and ion exchangers are used to achieve excellent results. 
     Other and further objects of the invention will be obvious upon an understanding of the illustrative embodiment about to be described, or will be indicated in the appended claims and various advantages not referred to herein will occur to one skilled in the art upon employment of the invention in practice. 
     The present invention accomplishes these objects by using the enzyme assisted transport of ions across a membrane against a concentration gradient, i.e., from a lower concentration to a higher one. The transport is powered through a chemical reaction, specifically the hydrolysis of ATP (adenosine 5&#39;-triphosphate) to ADP (adenosine 5&#39;-diphosphate) and P i  (inorganic phosphate). The preferred enzyme is designated Na + ,K +  -ATPase because its most common action is catalyzing the hydrolysis of ATP in powering the transport of Na +  ions from inside an animal cell across the cell membrane to outside the cell, almost simultaneous with transporting K +  ions from outside to inside. The biochemical equipment for this activity is known as the &#34;sodium pump&#34; or, more precisely, as the Na,K-pump. 
     The process utilizes (1) the Na,K-pump to transport Na +  ions with accompanying anions from water to be desalinated to a solution which may be discarded, and (2) ion exchangers to exchange other cations for Na +  which can then be removed from the water by the Na,K-pump. The method of the present invention is very efficient because the number of cations transported by the pump from inside to outside the membrane is substantially greater than the number brought back; whereas, ion exchangers exchange different species with the same charge one-for-one. 
    
    
     DRAWINGS 
     A preferred embodiment of the invention has been chosen for purposes of illustration and description and is shown in the accompanying drawing forming a part of the specification, wherein: 
     The single drawing FIGURE shows a schematic simplified plan view of the process of the present invention. 
    
    
     The following legend on the drawing will be useful in explaining the process of the present invention: 
     P--Pump to increase pressure to compensate for increased osmotic pressure from inside stream. 
     M--Na,K-pump membrane. 
     AE--Anion exchangers: 
     AE 1  --P i  removed and replaced by other anions. 
     AE 2  --ADP removed and replaced by other anions. 
     CE--Cation exchangers: 
     CE 1  --Other cations removed and replaced by Na +  only for stage 1. 
     CE 2  --K +  removed and replaced by Na + . 
     B--Connection for inside stream of stage 1. For other stages, inside stream is from outflow of previous stage. 
     At final stage for very pure water: in AE 2 , anions are replaced by OH -  ; and, in CE 2 , cations are replaced by H + . 
     DESCRIPTION 
     The process of the present invention utilizes the following ingredients: 
     1. Na + ,K +  -ATPase (Na,K-ATPase) which is found in cell membranes of mammals and many other animals. It may be extracted from the membranes, purified, and reestablished in manufactured lipid membranes with substantially the same activity as in the original membrane. Different species of Na,K-ATPase are found in different tissues. 
     2. The Na,K-ATPase must be placed in a membrane with necessary lipids, and must be oriented so that the major Na +  activation affinity is on one side of the membrane (like the inside of a cell), and the major K +  activation affinity is on the other (like the outside of a cell). The membrane must be strong enough to withstand the extra pressure exerted by the less concentrated solution and must be &#34;tight&#34; enough to adequately reduce ordinary diffusion from one side to the other of cations and water. 
     3. The most efficient cell activity of the Na,K-pump, powered by hydrolysis of ATP, is 
     
         3 Na.sup.+ (inside cell)+2K.sup.+ (outside cell)+ATP→3 Na.sup.+ (outside cell)+2K.sup.+ (inside cell)+ADP+P.sub.i, 
    
     in which both Na +  and K +  are moved from lower to higher concentrations. The Na,K-pump transport of 3 Na +  &#34;out&#34; coupled to K +  &#34;in&#34; is utilized because it transports Na+ much faster than other Na,K-pump arrangements. Other Na,K-pump reactions, in which other monovalent ions are substituted for K +  in its transport from outside to inside, are slower or less efficient. 
     4. ATP is the vehicle most used for transferring energy from biologic fuels to produce biochemical activity. It is available commercially, being used to inhibit enzymatic browning of raw edible plant materials, such as sliced apples, potatoes, etc. It can be synthesized or extracted from organic tissues. Energetically, upon hydrolysis 
     
         ATP←→ADP+P.sub.i +7300 calories (8.5 watt-hours). 
    
     5. Ion exchangers, either granular or membrane, can remove ions from a solution while giving to the solution other ions of the same charge. Ion exchangers are anionic or cationic, either naturally occurring or manufactured and they are available for many specialized exchange uses. 
     Referring to the drawing, seawater or brackish water is brought to the plant reservoirs. It is filtered and the flow of the filtered water is divided into two streams labeled &#34;outside&#34; and &#34;inside&#34;. The &#34;inside&#34; stream is to be desalinated. The &#34;outside&#34; stream is a vehicle to remove substances rejected from the inside stream. It may also be the same as a source of K +  for the Na,K-pump operation, or possibly, as a source of ions for regeneration of ion exchangers. 
     The cation concentration of seawater is approximately: Na + , 460 mM (millimolar); K + , 10 mM; Mg ++ , 52 mM; and other cations to total an equivalence of 590 to 600 mM. 
     The inside stream first enters a cation exchanger CE 1  where most of the cations other than Na +  will be exchanged for Na + , bringing the Na +  concentration (assuming a slight concentration from evaporation in the reservoirs) to 600 mM--plus a small Mg ++  concentration (needed for Na,K-pump activity) which will be disregarded in the following calculations. 
     The inside and outside streams will flow through the first Na,K-pump unit M. The inside stream will flow through the first Na,K-pump unit M. The inside stream has ATP continuously added from an outside source and flows on the side of the membrane M equivalent to the inside of a cell. The outside stream flows on the side of the membrane equivalent to the outside of a cell. Flow of the outside stream is kept adequate to furnish all the K +  necessary to balance 2/3 of the expected Na +  transport. Most of the Na +  from the inside stream is rejected into the outside stream; and the outside stream will have enriched the inside stream with K +  by a molar amount equal to 2/3 the moles of the Na +  transported out. Anions will have moved across the membrane to maintain equivalence to the cations. Added pressure is applied at intervals in the outside stream by the pump P to approximately compensate for the extra osmotic pressure across the membrane from the lower concentrations in the inside stream. 
     The outside stream is directed to a reservoir anion exchanger AE 1  for recovery of P i  (from the ATP hydrolysis), and to be used either to regenerate ion exchangers, to be returned to the sea, or to be otherwise discarded. The inside stream proceeds to a cation exchanger CE 2  where its K +  is mostly exchanged for Na + , and to an anion exchanger AE 2  to remove ADP for reconversion to ATP. Chemical methods for production of ATP from ADP and P i  are known. At this stage the inside stream is similar to when it entered the first Na,K-pump unit--but with only 2/3 the salt concentration. To continue with desalination of the inside stream, the same sequence of Na,K-pump elimination of Na +  followed by Na +  replacement of K +  through cation exchange CE 2  is repeated over and over to continually reduce the stream&#39;s ionic content. After 12 such paired treatments, but before the last cation exchange, the Na +  in the inside stream will be about 1 mM and the K +  about 5 mM. At this stage, both OH -  -conditioned anion exchanger and H +  -conditioned cation exchanger may be used for final deionization, regenerating the respective exchangers with base and acid. 
     For optimum operation certain conditions such as temperature and chemical concentrations are preferred. These may be regulated by standard procedures. 
     Using the process described, the total ATP requirement is 0.60 moles to desalinate a liter of water--2270 moles per 1000 gallons. 8.5 watt-hours will theoretically reassemble ADP and P i  into one mole of ATP; so 19.3 kWh would handle the Na,K-pump energy for 1000 gallons of desalinated seawater. With electrical energy at two cents a kWh and 48% efficiency of conversion, the energy would cost $0.80 per 1000 gallons. This does not include pumping, heating, etc., but only the cost of moving ions out of the water to be desalinated. 
     The energy requirement may be reduced by cation exchange of the outside stream: exchanging all the monovalent cations to Na +  --or to cations with charges greater than 1. It has been found that the Na,K-pump will function, although more slowly, under either of those conditions: with the only monovalent cation being Na +  outside the membrane, for every ATP hydrolyzed there are 3 Na +  ions transported out and only &#34;one to two&#34; Na +  ions transported back; with no monovalent cations, for every ATP hydrolyzed there are 3 Na +  transported out and zero cations back. 
     The energy requirement may be reduced if the ADP-ATP conversion requires less than double the free energy difference. The cost may be reduced if the conversion uses less expensive energy than electricity at $0.02/kWh. 
     Applications of the process include (1) deionizing solutions other than seawater, (2) bleeding off solutions as desired at different points of the process (e.g., only moderately deionized solutions for some commercial uses), (3) using the process as part of a multi-method system either parallel to or sequential with other methods. 
     In the process, speed or efficiency may be increased by appropriately modifying either or both of the incoming streams with ion exchange or dilution. 
     It is possible that some of the high energy phosphates other than ATP, such as the triphosphates of the nucleosides and deoxyribonucleosides (e.g., uridine triphosphate), might similarly to ATP if the appropriate enzyme-transport system were used. 
     Miscellaneous engineering hardware, including pumps, piping, reservoirs, heaters, instrumentation, and controls should not release certain substances (such as vanadium) to contact the Na,K-pump because of hazards to its activity; this may be controlled with appropriate ion exchangers. 
     It will be seen that the present invention provides an improved desalination method and means which uses a transport membrane to achieve excellent results, in which the exchange of ions across the membrane is sufficient for the replacement of more ions in one direction than in the other direction, in which the membrane is subject to increased pressure in order to permit more ions to be moved in one direction than in the other direction and in which the combination of a membrane and ion exchangers are used together to achieve excellent results. 
     As many and varied modifications of the subject matter of this invention will become apparent to those skilled in the art from the detailed description given hereinabove, it will be understood that the present invention is limited only as provided in the claims appended hereto.