Abstract:
Emulsification is achieved by directing a jet of fluid along a first path, and interposing a structure in the first path to cause the fluid to be redirected in a controlled flow along a new path, the first path and the new path being oriented to cause shear and cavitation in the fluid. A hot emulsion is stabilized immediately after formation by causing the emulsion to flow away from the outlet end of an emulsion forming structure, and causing a cooling fluid to flow in a direction generally opposite to the flow of the emulsion and in close enough proximity to exchange heat with the emulsion flow. In another aspect, emulsification of a first fluid component within a second fluid component is achieved by providing an essentially stagnant supply of the first fluid component in a cavity, and directing a jet of the second fluid component into the first fluid component, with the temperatures and the jet velocities of the fluids being chosen to cause cavitation due to hydraulic separation at the interface between the two fluids. In other aspects, a coiled tube is used to reduce pressure fluctuations in an emulsifying cell fed from a fluid line by a high pressure pump; A two-piece nozzle is used in an emulsification structure; an absorption cell has a reflective surface at the end of the chamber for reflecting the jet, and a mechanism is provided for adjusting the distance from the reflective surface to the open end; a modular emulsification structure includes a series of couplings that can be fitted together in a variety of ways.

Description:
BACKGROUND OF THE INVENTION  
         [0001]    This invention relates to forming emulsions.  
           [0002]    We use the term “emulsion” for a system comprising two immiscible liquid phases, with one phase dispersed as small droplets in the other phase. For simplicity we will call the dispersed phase “oil” and the continuous phase “water”, although the actual components may vary widely. As additional components, emulsifying agents, known as emulsifiers or surfactants, serve to stabilize emulsions and facilitate their formation, by surrounding the oil phase droplets and separating them from the water phase.  
           [0003]    The uses of emulsions have been increasing for many years. Most processed food and beverage products, medicine and personal care products, paints, inks, toners, and photographic media are either emulsions or employ emulsions. In recent years, demand for emulsions with smaller and more uniform droplets has increased. Artificial blood applications, for example, require nearly uniform droplets averaging 0.2 micrometers. Jet-ink printing has similar requirements of size and distribution.  
           [0004]    High pressure homogenizers are often used to produce small and uniform droplets or particles, employing a device which is commonly referred to as an homogenizing valve. The valve is kept closed by a plug forced against a seat by means of a spring or hydraulic or pneumatic pressure. The pre-mixed raw emulsion is fed at a high pressure, generally between 1,000 and 15,000 psi, to the center of the valve seat. When the fluid pressure overcomes the force closing the valve, a narrow annular gap (10-200 um) is opened between the valve seat and the valve plug. The raw emulsion flows through, undergoing rapid acceleration as well as sudden drop in pressure which breaks down the oil phase into small droplets. More recently, a new type of high pressure homogenizer was introduced, employing two or more fixed orifices, and capable of reaching 40,000 psi. When forced through these orifices, the pre-mixed raw emulsion forms liquid jets which are caused to impinge at each other. A description is found in U.S. Pat. Nos. 4,533,254 and 4,908,154.  
           [0005]    The typical mechanism for emulsification in this type of device is the controlled use of shear, impact, and cavitation forces in a small zone. The relative effects of these forces generally depend on the fluid&#39;s characteristics, but in the vast majority of emulsion preparation schemes, cavitation is the dominant force.  
           [0006]    Fluid shear is created by differential velocity within the fluid stream, generated by the sudden fluid acceleration upon entering the orifice or small gap, by the difference between the extremely high velocity at the center of the orifice and zero velocity at the surfaces defining the orifice, and by the intense turbulence which occurs after exiting the orifice.  
           [0007]    Cavitation takes place when pressure drops momentarily below the vapor pressure of the water phase. Small vapor bubbles form and then collapse (within 10-3 to 10-9 sec.), generating shock waves which break down surrounding oil droplets. Cavitation occurs in homogenizing valves when the sudden acceleration in the orifice, with a simultaneous pressure drop, causes the local pressure to drop momentarily below the vapor pressure.  
           [0008]    More generally, it has become known that cavitation occurs when two surfaces are separated faster than some critical velocity, and that cavitation bubbles affect their surrounding only during the formation of the cavities, and not during the collapse of the cavities, as had been long assumed. Another discovery of interest is that cavitation can occur either totally within the liquid, or at the solid-liquid interfaces, depending on the relative strength of solid-liquid adhesion and the liquid-liquid cohesion.  
           [0009]    Typical emulsification schemes have several characteristics worth noting. Cavitation takes place only once, for a very short time (10-3 to 10-9 seconds), and equipment which employs high power density imparts emulsification energy only to a very small portion of the product at any given time. The emulsification process is thus highly sensitive to the uniformity of the feed stock, and several passes through the equipment are usually required before the desired average droplet size and uniformity are achieved. The final droplet size depends on the surfactant&#39;s rate of interaction with the oil phase. Because surfactants cannot generally surround the oil droplets at the same rate they are being formed by the emulsifying process, agglomeration takes place and average droplets size increases. There is a typical sharp increase in product temperature during the process, which limits the choice of emulsion ingredients and processing pressure, as well as accelerating the agglomeration rate of the droplets after the emulsification process. Some processes require very small solid polymer or resin particles; and this is often accomplished by dissolving solid polymers or resins in VOC&#39;s (volatile organic compounds), then employing mixing equipment to reduce the droplets size, and finally removing the VOC.  
         SUMMARY OF THE INVENTION  
         [0010]    In general, in one aspect, the invention features a method for use in causing emulsification in a fluid. In the method, a jet of fluid is directed along a first path, and a structure is interposed in the first path to cause the fluid to be redirected in a controlled flow along a new path, the first path and the new path being oriented to cause shear and cavitation in the fluid.  
           [0011]    Implementations of the invention may include the following features.  
           [0012]    The first path and the new path may be oriented in essentially opposite directions. The coherent flow may be a cylinder surrounding the jet. The interposed structure may have a reflecting surface that is generally semi-spherical, or is generally tapered, and lies at the end of a well. Adjustments may be made to the pressure in the well, in the distance from the opening of the well to the reflecting surface, and in the size of the opening to the well. The controlled flow, as it exits the well, may be directed in an annular sheet away from the opening of the well. An annular flow of a coolant may be directed in a direction opposite to the direction of the annular sheet.  
           [0013]    In general, in another aspect, the invention features a method for use in stabilizing a hot emulsion immediately after formation. The emulsion is caused to flow away from the outlet end of an emulsion forming structure, and a cooling fluid is caused to flow in a direction generally opposite to the flow of the emulsion and in close enough proximity to exchange heat with the emulsion flow.  
           [0014]    Implementations of the invention may include the following features. The emulsion may be formed as a thin annular sheet as it flows out of the emulsion forming structure. The cooling fluid may be a thin annular sheet as it flows opposite to the emulsion. The cooling fluid may be a liquid or gas compatible with the emulsion. The flows of the emulsion and the cooling fluid may occur in an annular valve opening.  
           [0015]    In general, in another aspect, the invention features a method for use in causing emulsification of a first fluid component within a second fluid component. In the method, an essentially stagnant supply of the first fluid component is provided in a cavity. A jet of the second fluid component is directed into the second fluid component. The temperatures and the jet velocities of the fluids are chosen to cause cavitation due to hydraulic separation at the interface between the two fluids.  
           [0016]    Implementations of the invention may include the following features. The second fluid component may include a continuous phase of an emulsion or dispersion. The first fluid component may be a discontinuous phase in the emulsion, e.g., a solid discontinuous phase. The second fluid may be provided in an annular chamber, and the jet may be delivered from an outlet of an orifice which opens into the annular chamber. After emulsification by hydraulic separation, the product may be passed through an orifice to cause additional emulsification, or may be delivered to a subsequent processing chamber, where an additional component may be added to the emulsion. A cooling fluid may be applied to the product in the subsequent processing chamber to quickly cool and stabilize the emulsion. The subsequent processing chamber may be an absorption cell into which a jet of the product is directed.  
           [0017]    In general, in another aspect, the invention features an apparatus for reducing pressure fluctuations in an emulsifying cell fed from a fluid line by a high pressure pump. A coiled tube in the fluid line between the pump and the emulsifying cell has internal volume, wall thickness, coil diameter and coiling pattern adequate to absorb the pressure fluctuations and capable of withstanding the high pressure generated by the pump. The apparatus may include a shell around the coiled tube with ports for filling the shell with heating or cooling fluid.  
           [0018]    In general, in another aspect, the invention features a nozzle for use in an emulsification structure. In the structure, two body pieces having flat surfaces mate to form the nozzle, at least one of the members having a groove to form an orifice in the nozzle. The surfaces are sufficiently flat so that when the two body pieces are pressed together with sufficient force, fluid flow is confined to the orifice. In implementations of the invention, the cavitation inducing surfaces may be defined on the groove; and a wall of the groove may be coated with diamond or non-polar materials or polar materials.  
           [0019]    In general, in another aspect, the invention features an absorption cell for use in an emulsification structure. The cell includes an elongated chamber having an open end for receiving a jet of fluid having two immiscible components. A reflective surface is provided at the other end of the chamber for reflecting the jet. And a mechanism is provided for adjusting the distance from the reflective surface to the open end.  
           [0020]    Implementations of the invention may include the following features. The reflective surfaces may be interchangeable for different applications. There may be a removable insert for insertion into the chamber at the open end, the insert having an orifice of a smaller dimension than the inner wall of the chamber. There may be several different inserts each suitable for a different application.  
           [0021]    In general, in another aspect, the invention features a modular emulsification structure comprising a series of couplings that can be fitted together in a variety of ways. Each of at least one of the couplings includes an annular male sealing surface at one end of the coupling, and an annular female sealing surface at the other end of the coupling. An opening is provided between the male and female sealing surfaces, for communicating fluid from a up-stream coupling to a down-stream coupling. Ports are provided for feeding fluid into or withdrawing fluid from the coupling. At least some of the communicating openings are sufficiently small to form a liquid jet. The sealing surfaces are sufficiently smooth to provide a fluid-tight seal when the couplings are held together by a sufficient compressive force directed along the length of the structure.  
           [0022]    Implementations of the invention may include the following features. A processing chamber may be defined between the male sealing surface of one of the up-stream couplings and the female sealing surface of one of the downstream couplings. In some of the couplings, the orifice may extend from one end of the coupling to the other. An absorption cell coupling may be used at one of the structure. One of the couplings may extend into another coupling to form a small annular opening for generating an annular flow sheet of cooling fluid. Some of the ports in the couplings are used for CIP/SIP cleaning and/or sterilization procedures.  
           [0023]    Advantages of the invention include the following.  
           [0024]    Very small liquid droplets or solid particles may be processed in the course of emulsifying, mixing, suspending, dispersing, or de-agglomerating solid and/or liquid materials. Nearly uniform sub-micron droplets or particles are produced. The process is uniform over time because pressure spikes that are normally generated by the high pressure pump are eliminated. A broader range of types of emulsion ingredients may be used while maximizing their effectiveness by introducing them separately into the high velocity fluid jet. Fine emulsions may be produced using fast reacting ingredients, by adding each ingredient separately and by controlling the locations of their interaction. Control of temperature before and during emulsification allows multiple cavitation stages without damaging heat sensitive ingredients, by enabling injection of ingredients at different temperatures and by injecting compressed air or liquid nitrogen prior to the final emulsification step. The effects of cavitation on the liquid stream are maximized while minimizing the wear effects on the surrounding solid surfaces, by controlling orifice geometry, materials selection, surface characteristics, pressure and temperature. Absorption of the jet&#39;s kinetic energy into the fluid stream is maximized, while minimizing its wear effect on surrounding solid surfaces. A sufficient turbulence is achieved to prevent agglomeration before the surfactants can fully react with the newly formed droplets. Agglomeration after treatment is minimized by rapid cooling, by injecting compressed air or nitrogen and/or by rapid heat exchange, while the emulsion is subjected to sufficient turbulence to overcome the oil droplets&#39; attractive forces and maintaining sufficient pressure to prevent the water from vaporizing.  
           [0025]    Scale-up procedures from small laboratory scale devices to large production scale systems is made simpler because every process parameter can be carefully controlled. The invention is applicable to emulsions, microemulsions, dispersions, liposomes, and cell rupture. A wide variety of immiscible liquids may be used, in a wider range of ratios. Smaller amounts of (in some cases no) emulsifiers are required. Emulsions can be produced in one pass through the process. The reproducibility of the process is improved. A wide variety of emulsions may be produced for diverse uses such as food, beverages, pharmaceuticals, paints, inks, toners, fuels, magnetic media, and cosmetics. The apparatus is easy to assemble, disassemble, clean, and maintain. The process may be used with fluids of high viscosity, high solid content, and fluids which are abrasive and corrosive.  
           [0026]    The emulsification effect continues long enough for surfactants to react with newly formed oil droplets. Multiple stages of cavitation assure complete use of the surfactant with virtually no waist in the form of micelles. Multiple ports along the process stream may be used for cooling by injecting ingredient at lower temperature. VOC&#39;s may be replaced with hot water to produce the same end products. The water will be heated under high pressure to well above the melting point of the polymer or resin. The solid polymer or resins will be injected in its solid state, to be melted and pulverized by the hot water jet. The provision of multiple ports eliminates the problematic introduction of large solid particles into the high pressure pumps, and requires only standard industrial pumps.  
           [0027]    Other advantages and features will become apparent from the following description and from the claims. 
       
    
    
     BRIEF DESCRIPTION OF THE DRAWINGS  
       [0028]    [0028]FIGS. 1 and 2 are block diagrams of emulsification systems.  
         [0029]    [0029]FIGS. 3A and 3B are an end view and a cross-sectional view (at A-A of FIG. 3A) of an emulsifying cell assembly.  
         [0030]    [0030]FIG. 4 is a larger scale cross-sectional view (at BB of FIG. 3A) of the emulsifying cell assembly.  
         [0031]    [0031]FIG. 5 is a cross-sectional view of another modular emulsifying cell assembly.  
         [0032]    [0032]FIG. 6 is an isometric exploded view, not to scale, of two types of a two-piece nozzle assembly.  
         [0033]    [0033]FIGS. 7A and 7B are an enlarged end view and a cross-sectional view of an adapter for the two-piece nozzle assembly.  
         [0034]    [0034]FIG. 8 is a schematic cross-sectional diagram, not to scale, of fluid flow in an absorption cell.  
         [0035]    [0035]FIG. 9 is a cross-sectional view of an absorption cell.  
         [0036]    [0036]FIGS. 10 and 11 are cross-sectional diagrams, not to scale, of fluid flow in other modular absorption cell assemblies.  
         [0037]    [0037]FIGS. 12A, 12B and  12 C are an end view, a front view, and a top view of a coil for regulating process pressure in the emulsifying cell.  
         [0038]    [0038]FIG. 13 is an assembly of three coils shown in FIGS. 12A through 12C. 
     
    
     DESCRIPTION OF THE PREFERRED EMBODIMENTS  
       [0039]    In FIG. 1, the product ingredients are supplied from sources  110 ,  112 , and  114  into a pre-mixing system  116 . For simplicity, only three types of ingredients are shown by way of example: water, oil, and emulsifier; but a wide variety of other ingredients could be used depending on the product to be made. The pre-mixing system  116  is of a suitable kind (e.g. propeller mixer, colloid mill, homogenizer, etc.) for the type of product. After pre-mixing, the ingredients are fed into the feed tank  118 . In some cases, the pre-mixing may be performed inside feed tank  118 . The pre-mixed product from tank  118  then flows through line  120  and valve  122 , by means of transfer pump  124  to the high pressure process pump  128 . Transfer pump  124  may be any type of pump normally used for the product, provided it can generate the required feed pressure for proper operation of the high pressure process pump. Pressure indicator  126  is provided to monitor feed pressure to pump  128 . The high pressure process pump  128  is typically a positive displacement pump, e.g., a triplex or intensifier pump. From process pump  128  the product flows at high pressure through line  130  into coil  132 , where pressure fluctuations generated by the action of pump  128  are regulated by expansion and contraction of the coil tubing. A more detailed explanation of the coil mechanism is given in the description of FIGS. 12A through 12C. It may be desirable or necessary to heat or cool the feed stock. Heating system  148  may circulate hot fluid in shell  154  via lines  150  and  152 , or cooling system  156  may be used. The heating medium may be hot oil or steam with the appropriate means to control the temperature and flow of the hot fluid, such that the desired product temperature is attained upon exiting coil  132 . The product exits coil  132  through line  134 , where pressure indictor  136  and temperature indicator  138  monitor these parameters, and enters the emulsifying cell  140  at a high and constant pressure, for example a pressure of 15,000 psi.  
         [0040]    The emulsification process takes place in emulsifying cell  140 , where the feed stock is forced through at least one jet generating orifice and through an absorption cell wherein the jet&#39;s kinetic energy is absorbed by a fluid stream flowing around the jet and in the opposite direction. In each of the treatment stages (there may be more than two), intense forces of shear, impact, and/or cavitation break down the oil phase into extremely small and highly uniform droplets, and sufficient time is allowed for the emulsifier to interact with these small oil droplets to stabilize the emulsion.  
         [0041]    Immediately following the emulsification process, cooling fluid from cooling system  156  is injected into the emulsion via line  158 , cooling the emulsion instantly by intimate mixing of the cooling fluid with the hot emulsion inside emulsification cell  140 . Cooling system  156 , may be a source of cool compatible liquid (e.g., cold water) or of compressed gas (e.g., air or nitrogen), with suitable means to control the temperature, pressure and flow of the cooling fluid, such that the desired product temperature is attained upon exiting emulsification cell  140 . The emulsion exits the emulsification cell  140  through line  142 , where metering valve  144  is provided to control back-pressure during cooling, and ensuring that the hot emulsion remains in liquid state while being cooled, thereby maintaining the emulsion integrity and stability. Finally, the finished product is collected in tank  146 .  
         [0042]    In the system illustrated by FIG. 2, the product&#39;s continuous phase is supplied from supply  110  into feeding tank  118 , while other ingredients are supplied from sources  112  and  114  directly into the emulsifying cell  140 . Some ingredients may be mixed together to reduce the number of separate feed lines, or there may be as many feed lines as product ingredients.  
         [0043]    Water from tank  118  flows through line  120  and valve  122 , by means of transfer pump  124  to the high pressure process pump  128 . Elements  128  through  138 , and  148  through  158  have similar functions to the same numbered elements of the system of FIG. 1.  
         [0044]    Oil and emulsifier, each representing a possibly unlimited number and variety of ingredients which may be introduced separately, flow from sources  112  and  114  into emulsifying cell  140 , through lines  162  and  164 , each with a pressure indicator  170  and  172 , and a temperature indicator  174  and  176 , by means of metering pumps  166  and  168 . Metering pumps  166  and  168  are suitable for type of product pumped (e.g. sanitary cream, injectable suspension, abrasive slurry) and the required flow and pressure ranges. For example, in small scale systems peristaltic pumps are used, while in production system and/or for high pressure injection, diaphragm or gear pumps are used.  
         [0045]    Inside emulsifying cell  140  the water is forced through an orifice, creating a water jet. Other product ingredients, as exemplified by the oil and emulsifier, are injected into emulsifying cell  140 . The interaction between the extremely high velocity water jet inside emulsifying cell  140  and the stagnant ingredients from lines  162  and  164 , subjects the product to a series of treatment stages, in each of which intense forces of shear, impact, and/or cavitation break down the oil and emulsifier to extremely small and highly uniform droplets, and allows sufficient time for the emulsifier to interact with the oil droplets. Immediately following the emulsification process, the emulsion is cooled and then exits the emulsification cell and is collected, all in a manner similar to the one used in the system of FIG. 1.  
         [0046]    As seen in FIGS. 3 through 9, the emulsifying cell is constructed using a series of interchangeable couplings, each for a particular purpose. The couplings are used to form an integral pressure containing unit by forcing together a smooth and tapered sealing surface of each coupling into a smooth and tapered corresponding sealing surface in the adjacent coupling, to create a metal-to-metal seal, much like the seal between a standard high pressure nipple and the corresponding female port. Each coupling (except possibly for the end couplings) has a large bore in one side, and a matching protrusion of slightly smaller diameter on the other side, such that each coupling&#39;s protrusion fits into the bore of the next coupling, thereby aligning sealing surfaces and facilitating assembly of a large number of couplings. The couplings are fastened together by four bolts.  
         [0047]    In the example of a basic emulsifying cell shown in FIGS. 3A and 3B, the cell assembly has four couplings: product inlet coupling  10 , nozzle coupling  12 , coolant inlet coupling  14 , and product outlet coupling  16 . Referring also to FIG. 4, protrusion  26  of coupling  10  fits into bore  28  in coupling  12 , while sealing surface  22  of coupling  10  is aligned with sealing surface  24  in coupling  12 , to form a pressure containing metal-to-metal seal upon fastening of the assembly with four bolts  17 . The product fluid to be processed enters the emulsifying cell from port  18 , which is a standard ¼″ H/P port (e.g., Autoclave Engineers #F250C), and flows through round opening  20  (0.093″ dia. hole). Ejecting from opening  20 , the product impinges on surface  30  of coupling  12 , and then flows in a random turbulent pattern inside a generally cylindrical cavity  32 , which is formed between couplings  10  and  12 .  
         [0048]    Thus, from virtually zero velocity in the axial direction in cavity  32 , the product is accelerated to a velocity exceeding 500 ft/sec upon entering orifice  34 . This sudden acceleration which occurs simultaneously with a severe pressure drop causes cavitation in the orifice. Being a one piece metallic nozzle, coupling  12  is suitable for relatively low pressure applications in the range of 500 psi to 15,000 psi of liquid-liquid emulsions. Applications requiring higher pressure, or which contain solids, require a 2-piece nozzle assembly as shown in FIG. 6. The diameter of orifice  34  determines the maximum attainable pressure for any given flow capacity. For example a 0.015 in. diameter hole will enable 10,000 psi with a flow rate of 1 liter/min. of water. More viscous products require an orifice as large as 0.032 in. diameter to attain the same pressure and flow rate, while smaller systems with pumps&#39; capacity under  1  liter/min, require an orifice as small as 0.005 in. diameter to attain 10,000 psi. The high velocity jet is ejected from orifice  34  into an absorption cell cavity  38 , the flow pattern of which is shown in FIG. 8. An alternate absorption cell is shown in FIG. 9.  
         [0049]    Referring now to FIG. 8, water jet  35  formed in orifice  34  is maintained essentially unchanged as it flows through opening  36  of the absorption cell. After impacting surface  40 , which may be flat or semi-spherical, or have another configuration otherwise enhancing its function, the jet fluid reverses its flow direction, and forms a coherent cylindrical flow stream  37 . The cylindrical flow pattern is formed because that is the only way for the fluid to exit cavity  38 . With opening  36  only slightly larger than orifice  34 , fluid stream  37  is forced to react with the jet fluid  35 , thereby absorbing the kinetic energy of the jet fluid, generating intense forces of shear and cavitation, and minimizing the wear effect of the jet impacting on surface  40 . The intensity of energy input into the product is much lower in cavity  38  than in orifice  34 . Rather than further breaking down oil droplets, the interaction of the two streams in cavity  38  serves to provide sufficient time for the emulsifier to interact with the oil droplets formed in orifice  34  and completely surround them, thereby maintaining the oil droplets at the same small size achieved in orifice  34  and preventing their agglomeration. The absorption cell provides a controllable environment for the interaction to occur, depending on the diameter of the bore, the shape of the impact surface at the end of the cell, the length of the cell, and other design factors.  
         [0050]    Cavity  38  is formed inside stem  42 , which is threaded into outlet coupling  16  (FIG. 4). After exiting the cavity  38 , product flows between surface  44  of stem  42  and corresponding surface  46  in coupling  14 . The annular opening between surfaces  44  and  46  is adjusted by turning stem  42  in or out of coupling  16 , thereby controlling the back-pressure in cavity  38 . Stem  42  is provided with two flats to facilitate screwing it into coupling  16 , and with a lock-nut  48  for locking stem  42  in place. Port  50  is provided in coupling  14  for connection to a suitable cooling fluid supply. Cooling fluid flows through opening  52  and passes around “O”-ring  54 , which acts as a check-valve to prevent product flow to the cooling system. The cooling fluid then flows through a narrow annular opening formed between the tip of coupling  16  and surface  56  of coupling  14 , into cavity  58 . Thus, in cavity  58 , an annular flow sheet of cooling fluid interacts with an annular fluid sheet of hot emulsion, the two sheets flowing in opposite directions, thereby effecting intimate mixing and instantaneous cooling of the emulsion. The cooling fluid may be a compatible liquid or gas. For example, for oil-in-water emulsions, cold water may be used. In this case, the feed stock supplied to port  18  must contain a lower percentage of water, and the desired final oil/water ratio is accomplished by injecting the appropriate amount of cold water through port  50 . Alternatively, gas may be used as a cooling fluid. For example, compressed air or nitrogen may be supplied to port  50  under pressure, to be injected into cavity  58 , where the gas expansion from its compressed state requires heat absorption, thereby effecting instantaneous cooling of the hot emulsion. In this case, the air or nitrogen are released to atmosphere after the emulsion exits the emulsifying cell. From cavity  58 , the emulsion flows through annular opening  60 , to outlet port  62  which is a ¼″ H/P type. After exiting the emulsifying cell, the emulsion flows through a metering valve, provided to enable control of back-pressure in cavity  58  and to prevent “flashing” or sudden evaporation of liquid ingredient before temperature reduction.  
         [0051]    In the example of a more elaborate emulsifying cell shown in FIG. 5, multiple product inlet ports and multiple orifices are used. Couplings  10  and  12  are connected as described with respect to FIGS. 3 and 4. Couplings of the kind identified as  13 A and  13 B are provided to enable injection of other product ingredients through ports  72  and  74 , which are ¼″ H/P type, similar to port  18 . Coupling  13  may be installed before or after coupling  12 , or before or after coupling  15 , in conjunction with one or more orifices, all depending on the particular product characteristics and the desired results. Nozzle adapter  70  is provided to enable high-pressure sealing between couplings  12  and  13 A. Coupling  13  may be connected to another coupling  13  or to coupling  14  without any adapters. Coupling  15  contains a 2-piece nozzle assembly. Nozzle adapter  84  enables high-pressure sealing between the two orifice pieces  80  and  82 , as well as between the 2-piece nozzle assembly and the coupling down-stream.  
         [0052]    The product&#39;s continuous phase, water for example, is fed at high pressure through port  18  and then forced through orifice  34 , thereby forming a water jet. Another ingredient, oil for example, is fed through port  72  at an appropriate pressure and temperature. The required oil pressure is a function of inlet water pressure at  18 , the size of the orifice  34 , and the size of the orifice formed by members  80  and  82 . For example, using water pressure of 20,000 psi at  18 , orifice of 0.015 in. dia. at  34 , and round orifice of 0.032 in. dia. by members  80  and  82 , then water pressure between the two orifices is slightly below 4,500 psi, and thus oil pressure of 4,500 is required at port  72  to assure oil flow into the emulsifying cell. At the interface between the water phase and oil phase, cavitation takes place due to hydraulic separation, effecting a homogeneous oil in water mixture at the exit of coupling  13 A. The orifice formed between members  80  and  82  causes further break down of oil droplets, due to the severe acceleration with simultaneous pressure drop and due to orifice geometry. After this intense energy input, another product ingredient is added through port  74 , for example emulsifier, which interacts with the process jet in a manner similar to the interaction between oil and water described above. The required feed pressure at port  74  is determined by the adjustment of stem  42 , and will be generally in the range of 50 psi to 500 psi. This relatively low feed pressure enables use of ingredients that are difficult or impossible to pump with the high pressure process pump. For example, extremely viscous products and abrasive solids which would cause rapid wear to the plunger seals and check-valves of the high pressure pump, could be supplied to port  74  with standard industrial pumps. Port  74  may be also used for feeding melted polymers or resins, to be emulsified in liquid state into water, thereby replacing a common use of VOC&#39;s.  
         [0053]    In the two different two-piece nozzle arrangements shown in FIG. 6, the orifice is formed as an open groove on the face of each nozzle member, thereby enabling fabrication of intricate orifice geometries and facilitating coating with suitable materials. For example, when members  80  and  82  are pressed together, they form a rectangular cross section orifice, with surfaces  86  and  88  of member  82  being optically flat (within 1 light band), forming a pressure containing seal with the corresponding surfaces of member  80 . Surface  90  forms a step along the flow path in the orifice and serves to induce cavitation. The location of surface  90  along the orifice may be chosen to induce cavitation at the entrance of the orifice or at its exit, depending on the configuration of the emulsifying cell. Additionally, various slope angles of surface  90  and of the step formed after it may be used to control the rate of cavity formation and collapse, all depending on the product characteristics and desired results. The nozzle assembly made of members  92  and  94  will be essentially the same as a round hole in a solid block, but the two-piece construction allows coating of the inner surface the extremely small orifice with materials such as diamond, thereby enabling continuous production of abrasive products at high pressure. Such a scheme would be useful for producing small solid particles of materials such as ceramics or iron-oxide for magnetic media.  
         [0054]    As seen in FIG. 5, the two nozzle members  80  and  82  are inserted into a bore in a nozzle adapter  84 . The nozzle adapter is shown in greater detail in FIGS. 7A and 7B. Upon fastening the emulsifying cell assembly, the two nozzle members  80  and  82  are forced against surface  190  of adapter  84 , while the adapter tapered sealing surface  188  is forced against the adjacent coupling ( 13 B in FIG. 5). The axial compressive force on surface  188  has an inward radial component, which is transmitted through surface  186  to the two nozzle members  80  and  82 , thereby effecting a pressure containing seal between the members  80  and  82 . Slots  194  and  196  are provided to facilitate the translation of axial compression to radial compression of adapter  84 . Round hole  192  is provided for product flow.  
         [0055]    In the example of a more elaborate absorption cell shown in FIG. 9, the length of the cell and its effective internal diameter may be varied. Stem  242  has the same external dimensions as stem  42  in FIGS. 3, 4 and  5 , thus stems  42  and  242  are interchangeable. Stem  242  is provided with a smooth internal bore  238  at one end, internal threads at the other end, and a tapered sealing surface  208  in between. Nozzle insert  200  is fitted into the stem bore  238 , secured by such means as press-fitting or adhesive material, to form the cavity opening  236 . The use of inserts with a variety of lengths, internal surface geometry and size, enables control of the shear rate, cavitation, turbulence, and the impact at surface  240 . Rod  202  is inserted into stem  242  to provide the impact surface  240  of the absorption cell. The depth of cavity  238 , as determined by the positioning of rod  202 , controls the residence time of product in the absorption cell, which in turn enables providing sufficient interaction time between emulsifier and oil droplets. Sleeve  204  is provided to lock rod  202  in place, as well as to provide sealing between rod  202  and stem  242 . Once the location of rod  202  is selected, sleeve  204  is tightened. Tapered sealing surface  206  of sleeve  204  is then pressed against tapered sealing surface  208  of stem  242 , thereby forming a seal between sleeve  204  and stem  242 , as well as between sleeve  204  and rod  202 . Graduation marks at the exposed end of rod  202  facilitate accurate positioning of the rod and provide a convenient scale for recording.  
         [0056]    The two absorption cell assemblies in FIGS. 10 and 11 exemplify a large variety of ways to accommodate particular product requirements. Nozzle inserts  300 ,  302 A,  302 B and  304  are examples of a large variety of inserts that may be used. The generally concave internal opening of insert  300  induces cavitation when fluid enters cavity  306 . The fluid immediately near surface  308  will flow along a path defined by that surface, tending to separate form the flow path defined by the previous surface  310 . With simultaneous pressure drop resulting from the larger cross-section area of cavity  306 , cavitation occurs. The generally convex internal opening of insert  304  (FIG. 11) induces cavitation in the fluid stream upon exiting the insert. Fluid pressure is increased momentarily when fluid passes through the center of insert  304 . As in insert  300 , the fluid&#39;s tendency to follow the shape of the solid surface with a simultaneous pressure drop induces cavitation. Inserts  302 A and  302 B are identical and are arranged to achieve desired results for a particular product. Several identical inserts such as  302  may be used together, end-to-end, to form one continuous internal bore. Alternatively, several inserts with different internal diameters may be used to induce turbulence in the exiting fluid stream. Yet another alternative, shown in FIG. 10, is to leave a small space between the inserts to disrupt laminar flow and generate turbulence. Yet another alternative is to use several inserts such as  300  and/or  304  in series. In FIG. 11, reflecting surface  440  exemplifies a large variety of shapes that may be used to enhance its function or for a particular application. As compared with semi-spherical or flat reflecting surfaces, surface  440  has a much larger surface area reflecting the jet fluid. Such a scheme may be used to effect a more gradual flow reversal, and for abrasive solids applications for extending the service life of the reflecting surface.  
         [0057]    The coil shown in FIGS. 12A through 12C is used for removing pressure fluctuations (item  132  in FIGS. 1 and 2). The coil is made of standard high pressure tubing (E.g., Butech ¼″ M/P, #20-109-316), with coil diameter sufficiently large as not to effect significantly the pressure rating of the tubing (e.g., 4 in.), and of sufficient length to remove the pressure spikes (e.g, 60 ft.). The tubing expands slightly when the pump generates a pressure spike, thereby acting to absorb the excess energy generated by the pressure spike. At the end of the pressure spike, the tubing contracts, thereby releasing the stored energy. This action of the coil is similar to the action of standard hydraulic accumulators that are used in hydraulic systems for essentially the same purpose. Waterjet cutting systems employ similar principle (e.g. Flow International Corp.&#39;s “Attenuator”), in the form of a long straight cylinder between the high pressure intensifier pump and the nozzle, for generating constant flow rate through the nozzle. As can be seen in FIGS. 12A through 12C, the tubing is coiled in a way that allows each coil ring to flex in response to pressure fluctuations, in a similar action of a Bourdon tube (used in pressure gauges). Because the external side of each coil ring has a larger area than the internal side, pressure in the tubing tends to open each ring. This movement in response to pressure fluctuations provides another mechanism for absorbing and releasing energy. The coil thus provides means for removing pressure fluctuations, heating or cooling the product, while being suitable for CIP/SIP sterile systems. FIG. 13 illustrates a scheme for connecting several coils such as in FIGS. 12A through 12C, enabling the use of standard tubing length (e.g. 20 ft.) and standard bending tools to produce coils as long as necessary.  
         [0058]    Other embodiments are within the scope of the following claims.