US 5,045,213 AGrant
Waste Water Treatment Method and Apparatus
Issue Date:1991-09-03
•30 Claims
•2 Drawing Sheets
Abstract
Waste water treatment for the removal of heavy metals is optimized by continuously removing and filtering a sample flow of treated waste water subject to pH level control to determine the presence of remaining metals in solution to be precipitated. Filtering of the sample removes metals precipitated by pH level control. Optimized pH level control can cause precipitation of most non-chelated and/or non-complexed metals, so that controlled feeding of a precipitating agent, preferably a calcium dithiocarbamate, to the treated waste water is effectively determined by only those metals remaining in solution, which are typically either chelated and/or complexed heavy metals. The filtered sample is injected with a diluted solution of the precipitating agent, and then a turbidity meter is used to determine the degree of turbidity of the injected clear sample. The resulting degree of turbidity corresponds to the level of precipitation caused by injection of the diluted precipitating agent. The precipitation level is in turn in direct correspondence with the level of remaining metals in solution. Differentiation between types of metals for control of feeding of the precipitating agent to the waste water permits optimized use of the precipitating agent, and minimized sludge production accompanying use of the precipitating agent.
Metadata
Assignee
- Southern Water Treatment Company, Inc.
Inventor
- Gregory S. Bowers
Application Information
Application Number:US 4791797
Filing Date:1990-02-13
Priority Date:1988-06-10
Art Unit:138
Classifications
IPC:
C02F 162
Field of Search:
210743;745;709;719;720;724;725-729;746;757;764;765;912-914;96.1;108;143;195.1 ;205;206;251;257.1;258;323.2;333.01;340;928
Patent Drawings (2 sheets)
Description
Brief Description of the Drawings
A full and enabling disclosure of the present invention, including the best mode thereof, is set forth below, in conjunction with reference to the accompanying figures, in which:
FIG. 1 comprises a block diagram representation of one embodiment in accordance with the present invention;
FIG. 2a comprises a block diagram representation of one embodiment in accordance with the present invention of the testing and control means of FIG. 1;
FIG. 2b comprises a block diagram representation of an alternative embodiment to that of FIG. 2a, for the testing and control means of present FIG. 1; and
FIG. 3 comprises a diagrammatical view of a multi-stage waste water treatment system incorporating heavy metal waste water treatment features in accordance with the present invention.
Repeat use of reference characters throughout the following specification and accompanying figures is intended to represent same or analogous features, elements, or aspects of this invention.
Detailed Description of the Preferred Embodiments
In conjunction with the following description of exemplary embodiments of this invention, it is to be understood that features and aspects of this invention may be variously practiced in combination with a variety of waste water treatment systems, not all of which are necessarily shown nor explicitly mentioned hereinafter. However, specific exemplary embodiments are presented herewith and discussed in detail below to provide those of ordinary skill in the art with an adequate disclosure of this invention for practicing same, either as shown and discussed herein or as adapted by such persons from time to time for conformance with their particular requirements.
As relates to waste water treatment, one aspect of this invention as represented by present FIG. 1 is that a filtered sample of waste water is obtained and monitored for determining controlled feeding of a given precipitating agent. Such methodology, even if readily accomplished with individual components which independent of one another are previously known, advantageously permits chemical feed operations based on information about metals remaining in solution to be precipitated.
With reference to FIG. 1, a process medium 10 is generally representative of a waste water treatment system, or at least a portion thereof such as a main treatment tank. The present invention is equally well practiced with a fixed body of waste water, such as may be contained in process medium 10, or (as is also typical in many waste water treatment systems) a process medium having a continuous inflow 12 and outflow 14. Such inflow and outflow may represent input to a waste water treatment system and discharge therefrom, respectively, or may represent flow connections with relative upstream and downstream stages of a multi-stage treatment system.
Where process medium 10 represents a body of waste water having metals in solution therewith to be precipitated as treatment thereof, such controlled body of waste water is preferably sampled, such as with sample flow 16. Sample flow 16 may be variously established, such as with a gravity feed tube or pipe. Alternatively, sampling flow or means 16 may incorporate use of a recirculating pump (not shown). Those of ordinary skill in the art will understand that various gravity feed and/or pump feed arrangements may be used interchangeably at different points in the systems disclosed herewith, without departing from the spirit and scope of the present invention.
Sampling means 16 establishes a preferably continuous sample flow from waste water in process medium 10. As discussed above, pH level control (not shown) or other preliminary treatment(s) may be practiced in process medium 10 (or stages upstream thereof) for precipitating non-chelated and/or non-complexed metals therefrom. The sample flow established with sampling means 16 includes such already precipitated metals in the treated waste water. Such treated waste water passes through liquid-solid separation means 18 which substantially removes such already precipitated metals from the sample flow so as to provide a clear sample. Such clear sample is present in flow line 20, while flow line 22 provides return means for recirculating the sample flow to process medium 10.
The clear sample forming output 20 of separation means 18 has substantially all of the already precipitated metals removed therefrom, but may contain further metals in solution therewith. For example, should process medium 10 contain waste water with chelated and/or complexed heavy metals in solution therein, pH treatment will not typically precipitate such heavy metals. Since such heavy metals remain in solution, they are passed through separation means 18 and continue in solution with the clear sample present in flow line 20. Thus, testing and control means 24 are advantageously operative on and actuated by only those metals which remain in solution after obtention of the above-mentioned clear sample. Where the pH level in process medium 10 is controlled with conventional technology (examples of which are given above in the Background portion of this specification) for effectively precipitating non-chelated and/or non-complexed metals, testing and control means 24 will be operative on and actuated by essentially only heavy metals which are chelated and/or complexed.
As represented by electric control line 26, testing and control means 24 operate a precipitating agent controlled pump means 28 for selectively feeding stored precipitating agent 30 to process medium 10 (i.e., the controlled body of waste water) via flow paths (e.g., tubing) 32 and 34. Essentially, testing and control means 24 tests the clear sample present in flow line 20 for the presence of any remaining metals in solution therein, and then feeds a given precipitating agent 30 to the controlled body of waste water (i.e., process medium 10) in response to the presence of such remaining metals so as to substantially precipitate same. Thus, various types of metals are substantially precipitated from the waste water in process medium 10, with controlled, minimized feeding of stored precipitating agent 30. Waste water passed through testing and control means 24 is also returned to process medium 10, via flow path 36.
By taking a sample from the controlled body of waste water, and obtaining a clear sample therefrom (preferably a continuously filtered sample), controlled feeding of the precipitating agent may be predicated upon metals remaining in solution. By proper (preferably optimum) control of the pH level in process medium 10, such remaining metals in solution will substantially comprise only chelated and/or complexed heavy metals. Therefore, operation of testing and control means 24 on such clear sample enables effective control of stored agent 30 for feeding thereof to process medium 10 for precipitating chelated and/or complex metals therefrom, while minimizing sludge production and precipitating agent overfeed.
FIGS. 2a and 2b are diagrammatic representations of alternative embodiments for testing and control means 24 of present FIG. 1. In the embodiment of FIG. 2a, the clear sample present in flow line 20' is passed through a continuous metal analyzer means 38. A return flow is again established to process medium 10 (or some other portion of the waste water treatment system) through flow line 36', so that the waste water itself remains in a closed treatment system. The continuous metal analyzer means may comprise any one of a variety of self-contained devices available in the marketplace, such as for testing for the presence of nickel, copper, or the like. One example is Model 61700-02 Trace Pump Analyzer by Hach Company, Loveland, Colo. 80539.
Details of analyzer means 38 do not form particular aspects of the present invention, and hence need not be specifically discussed in connection with an adequate disclosure of this invention. Such analyzer means produces a feedback signal 26' to which feeding control means 40 is responsive for in turn outputting a pump means control signal 42 for operation of a precipitating agent controlled pump means, such as pump means 28 of FIG. 1. Feeding control means 40 may comprise a variety of self-contained controllers available on the marketplace. One example of such a controller is the AMF-Cuno Sentrol controller, a precision control product available from the company at 400 Research Parkway, Meridan, Conn. 06450.
Setpoint or proportional control operations may alternatively be practiced. In setpoint control, a precipitating agent is fed to process medium 10 only whenever the detected level of metals in solution in the clear sample exceeds a predetermined setpoint. In proportional control, the amount of precipitating agent fed to the process medium is modulated in proportion with the degree of detected metals in solution in such clear sample.
A variety of chemical metering pumps are available on the market for operation with control means, under either setpoint control or proportional control operations. For example, the 1200P and 12000PHO series chemical pumps, available from Chem-Tech International, Inc., at 92 Bolt Street, Lowell, Mass. 01853, are made for use with the Sentrol controller noted above.
FIG. 2b illustrates an alternative embodiment for testing and control means 24, for use instead of the continuous metal analyzer means 38 of present FIG. 2a. In such alternative embodiment, the clear sample present in flow line 20" is injected with (preferably continuously) an indicator solution. Stored indicator solution 44 is fed by indicator solution injection pump means 46 into flow line 20" at an injection point 48 therein. While a variety of indicator solutions may be used, such solution preferably comprises the same precipitating agent which comprises stored agent 30 in present FIG. 1. In particular, the indicator solution may comprise a diluted strength of such precipitating agent.
Whenever a precipitating agent is applied (or fed) to the clear sample in flow line 20", metals remaining in solution in the waste water contained in such flow line (which as discussed above in connection with optimized pH level control are likely to be chelated and/or complexed heavy metals) react by being precipitated. Such precipitation turns the clear sample turbid to a degree corresponding to the degree that such precipitation occurs. Such degree of precipitation in turn directly corresponds with the amount of metal remaining in solution available to the precipitated. Thus, downstream from injection point 48 (where indicator solution 44 is fed into the sample flow in flow line 20"), turbidity (e.g. brownness or cloudiness) of the continuous sample flow may be detected for determining the corresponding degree to which metals remain in solution in the treated waste water (i.e. process medium 10).
Turbidity meter means 50 is used for detecting the degree of turbidity caused by injection of the indicator solution (i.e. diluted precipitating agent), for outputting a feedback signal 26" for input to feeding control means 40'. Such control means 40' may be substantially the same as control means 40 in the embodiment of FIG. 2a, and hence itself outputs a pump means control signal 42' analogous to signal 42.
A variety of turbidity meters are available in the marketplace, and may be utilized as turbidity meter means 50 in accordance with the present invention. An example of such a generally available turbidity meter is Model 1720C Turbidimeter by Hach Company, P. 0. Box 389, Loveland, Colo. 80539. Similar to the embodiments of FIGS. 2a and 1, a return flow path 36" from the turbidity meter means ensures that all the waste water remains in a closed system, i.e., is returned to process medium 10 or elsewhere in the treatment system.
By testing a clarified or filtered sample, whether with the embodiment of present FIG. 2a or present FIG. 2b or some equivalents thereof, a continuous process is provided which enables controlled feeding of a precipitating agent to the process medium to be based on the heavy metal concentration remaining in solution in such process medium. By so distinguishing between different types of metals in solution, use of the precipitating agent may be minimized, resulting in minimized sludge production and lowest chemical cost. Furthermore, by selection of the feedback signal characteristics and other operating parameters, the invention may be practiced for maintaining a certain turbidity level, and hence maintaining a corresponding heavy metal concentration in the process medium.
Various precipitating agents are available in the marketplace, and may be practiced in accordance with the present invention. One example of one of the preferred precipitating agents is sodium dimethyldithiocarbamate (hereinafter "DTC"). Another exemplary preferred precipitating agent is sodium borohydride. Examples of other chemicals useful in the removal of chelated and/or complexed heavy metals are: ferrous sulfate, sodium hydrosulfite, starch xanthate, sodium sulfide, magnesium oxide, and parasulfate.
Those of ordinary skill in the art will appreciate that a variety of factors may contribute to selection of a particular precipitating agent for use in accordance with the present invention. Additionally, use of a selected precipitating agent may dictate a particular regimen for preliminary pH level control in a multi-stage treatment system, as generally outlined above. For example, parasulfate is generally effective as a precipitating agent whenever the pH level is below 4. In order to precipitate those non-chelated and/or non-complexed metals which through pH level adjustment may be precipitated, the pH level of the waste water in one stage might be raised (such as up to 8.5 or 9), followed by a flocculation stage, followed by an adjustment of the pH level down to 4 or below to prepare for the controlled feeding of parasulfate. All such variations and modifications involving selection of particular precipitating agents, indicator solutions, corresponding pH level control, and the like are intended to come within the broader teachings of the present invention, with recognition that those of ordinary skill in the art may practice such modifications in accordance with this invention to accommodate their particular waste water treatment needs.
Another exemplary presently preferred embodiment in accordance with the present invention is disclosed hereinafter with reference to FIG. 3. Such FIG. 3 represents a waste water treatment process or system having a plurality of consecutive stages. Such multiple stage systems are generally known, and typically provide a continuous treatment facility accommodating an inflow 100 of collected waste water (such as gathered from various points about a commercial plant), and outputs including for example treated effluent 102 which may be connected to a commercial sewer, and sludge 104 which may be further processed in a press or the like.
In the multi-stage process represented in present FIG. 3, a main treatment tank 106 corresponds generally with process medium 10 of present FIG. 1 (i.e., main treatment tank 106 constitutes one source of waste water from which a sample may be withdrawn in accordance with the present invention). In the representative multi-stage system of present FIG. 3, situated upstream of such main treatment tank 106, and providing inflow thereto, is an equalization stage 108. Downstream from main treatment tank 106, and accepting outflow therefrom, are consecutively a coagulation stage 110, a flocculation stage 112, and a clarification stage 114. Operations of such stages 108, 110, 112, and 114, and other typical treatment system stages, are generally known to those of ordinary skill in the art and do not form particular aspects of the present invention; hence, detailed explanation thereof is not required herewith for a complete understanding of this invention.
While in one aspect the present invention concerns the overall combination of the process and system represented by the entirety of FIG. 3, in another, aspect, the present invention separately concerns the combination of apparatus illustrated in FIG. 3 beneath stages 106-114 (and the corresponding method of operation thereof).
Such apparatus includes tubing means 116 for establishing a preferably continuous sample flow from main treatment tank 106. While a gravity-dependent flow system may be utilized in whole or in part, a recirculating pump 118 is illustrated in FIG. 3 as representing pump-assisted alternatives to such gravity dependency.
Similar to operation of the embodiment of present FIG. 1, the continuous sample flow is passed through liquid-solid separation means 120 to substantially remove any already precipitated solids therefrom. Such solids most likely may comprise non-chelated and/or non-complexed metals already precipitated by pH level control treatment of the waste water in main treatment tank 106 (as discussed above in connection with such pH level control in process medium 10 of present FIG. 1).
In the exemplary embodiment of present FIG. 3, the basic aspect of separation means 120 is filter means 124, which as illustrated preferably comprises a pair of tubular filters 126 and 128 variously interconnected for passage of the continuous sample flow of waste water therethrough. While alternative filter means may be practiced in accordance with the present invention, ultra-filtration members comprising filter modules, such as the "Microdyn" membrane modules made by ENKA, are preferred since they permit relatively continuous filtering of the sample flow. The minimum particle trapping size of tubular filters 126 and 128 may vary, but preferably falls generally in a range from about 0.2 microns to about 5 microns. The selection of a trapping particle size may vary depending on circumstances of a given installation, and is thus in part left to preference or needs of particular users.
As illustrated in present FIG. 3, separation means 120 further includes a plurality of controllable valves 130 which may be controlled and operative, in combination with the tubing interconnecting same, for directing the sample flow of treated waste water through tubular filters 126 and 128 in either longitudinal direction thereof. Controllable valves 130 may be either manually or automatically controlled for periodically reversing the direction of flow through filters 126 and 128 (i.e., periodically backwashing the filters), which advantageously contributes to relatively prolonged periods of continuous operation without blockage of the filtering membranes of such tubular filters.
Furthermore, controllable valves 132 and 134, upstream and downstream respectively of separation means 120, may be appropriately controlled for isolating separation means 120 from sample tubing means 116 and return flow tubing 136 (which is part of the closed system for the waste water in the apparatus of the present invention). Once so isolated at controlled periodic intervals, clean external water from an available source such as tubing 138 may be supplied through a further controlled valve 140 for backwashing tubular filters 126 and 128, which also prevents clogging thereof.
Intermittent or periodic backwashing may occur under the control of an input interface control means 142, as illustrated. Such control means 142 comprises a centralized control means (such as a Sentrol controller, discussed above) for the FIG. 3 embodiment, and is further connected with other features and elements thereof for receiving feedback signals and outputting control signals, as discussed hereinafter.
Continuously filtered sample flow from separation means 120 is fed via flow line 144 through another controlled valve 146 (which is also controlled by control means 142 during backwashing for isolation of separation means 120) towards turbidity meter 148. Prior to passing through turbidity meter 148 (or turbidimeter), indicator solution 150 (such as a diluted strength of a precipitating agent such as DTC) is injected, by an indicator solution injection pump means 152, into the filtered continuous sample flow at an injection point 154 thereof. Thus, as discussed in connection with the above-described exemplary embodiments of the present invention, turbidity meter 148 may detect the turbidity (i.e., cloudiness) of the filtered continuous sample flow at a point downstream from injection point 154, and determine therefrom the corresponding degree to which metals remain in solution in main treatment tank 106. Another return flow path 156 returns the sample flow to main treatment tank 106 after it is injected with the indicator solution and tested with the turbidity meter.
Turbidity meter 148 may comprise any generally available turbidity meter means, such as discussed above in connection with the exemplary embodiment of present FIG. 2b. Turbidity meter 148 provides output (or feedback) signals on lines 158 and 160, which signals ultimately provide for controlled pumping of stored precipitating agent 162 to main treatment tank 106. Control means 142, which actually receives and responds to the turbidity level feedback signals on lines 158 and 160, may comprise an adapted Sentrol controller, as discussed above in connection with control means 40 and 40' of FIGS. 2a, and 2b respectively. Use of a Sentrol controller, or its equivalents, in accordance with the present invention falls generally within the abilities of those of ordinary skill in the art, without further detailed discussion thereof.
Selectively operating under either setpoint control or modulated control, control means 142 outputs a pump means control signal via line 164 to a pump controller 166, which appropriately commands chemical feed pump 168 to feed precipitating agent 162 into return flow line 136. Thus, the precipitating agent 162 is controllably fed into main treatment tank 106 in accordance with the detected need for further precipitation of metals in solution in such main treatment tank, beyond the pH induced precipitation thereof discussed above.
While general features and operative characteristics of the present invention have been discussed above in conjunction with the exemplary embodiment of present FIG. 3, various particular operating parameters thereof may be selected by those of ordinary skill in the art for use in particular applications. For example, backwashing control may be initiated at selected intervals, such as a period of one minute every hour or the like.
Moreover, various alarms 170 and 172 may be utilized for signalling an operator whenever the system fails to maintain the concentration of metals in solution in treatment tank 106 to within a predetermined maximum level. Actuation of the alarms may also be accompanied by various other automatic operations. For example, sensing of a defined excessive turbidity level might cause shut off of inflow waste water into tank 106 until the situation is rectified. Alarms can be triggered whenever separation means 120 becomes clogged such that the flow rate therein is less than a predetermined minimum level. Such information could be obtained with a conventional flow rate meter (not shown) or the like variously incorporated into the tubing of separation means 120, or at the inflow or outflow thereof. Typically, a continuous sample flow rate may be generally within a range of from about 1 to about 20 gallons per minute.
Depending upon applicable regulations, or other factors, the predetermined maximum setpoint concentration of metals in solution in main treatment tank 106 may be established generally in a range of from about 0 to about 5 parts per million. Likewise, the controlled level of pH in such treatment tank 106 may be varied depending on a variety of factors, such as the anticipated waste water matrix. For example, where waste water entering main treatment tank 106 contains anywhere from about 10 to about 300 parts per million of nickel, copper, or the like, a controlled level of pH in a range of 9 to 10 may precipitate most of the metal which is not chelated and/or complexed.
The most effective pH level which results in the least amount of sludge production will vary depending on the nature of the metals in solution, as understood by those of ordinary skill in the art. For example, copper will precipitate naturally at a pH of about 8.3, while zinc naturally precipitates at a level of about 10.2, and nickel precipitates at a level of 10.75. Particular controlled use of the precipitating agent in accordance with the present invention can be used to compensate for pH levels which deviate from ideal for particular types of metals. Such deviation can uncontrollably occur for a variety of reasons, including for example, lack of knowledge about the types of metals present in the waste water and/or continuous changing in the mix of metals in solution.
In addition to variety in the various features discussed above, alternative structural constructions may be practiced in accordance with the present invention. For example, while two tubular filters are illustrated in parallel in the exemplary embodiment of present FIG. 3, fewer or greater numbers of such filters (or substitutes therefor) may be practiced. Moreover, alternative backwashing arrangements may be practiced. For example, a plurality of selectable banks of tubular filters may be set up, with alternative sample flow therethrough so that "unused" tubular filters may in the meantime be thoroughly backwashed for subsequent use.
In addition to the foregoing modifications and variations, and others that will be readily appreciated by those of ordinary skill in the art, the present invention may be used in conjunction with processes other than waste water treatment. For example, one preferred precipitating agent, DTC, is also effective as a biocide, for killing organic or microbiological activity in various aqueous suspensions. Microbiological activity in cooling water towers can cause a variety of problems, such as inhibited heat transfer, and excessive corrosion, slime or algae growth. Similar growth activity in aqueous suspensions in papermaking or suspensions in sugar-making are also problematic.
The present invention may be practiced for controlling the feeding level of the consumable agent in such processing, which is variously consumed such as by precipitating metals in solution, or by encountering and killing organic or microbiological growth present in a given aqueous suspension. For example, a given indicator solution comprising heavy metals may be injected into a clear sample flow, in accordance with the present invention, for determining the degree to which the consumable agent remains in the aqueous medium. In other words, the role of heavy metals is essentially reversed in some applications from that discussed above in connection with FIG. 1-3. With this invention, the level of the biocide in the suspension can be monitored and regulated as desired without affecting the continuous process in which the aqueous suspension is otherwise involved.
Additionally, other dithiocarbamates, particularly group II metal dithiocarbamates and most particularly calcium dimethyldithiocarbamate (Ca(DTC).sub.2), are useful as biocides and, also, in the removal of chelated and/or complexed heavy metals such that they are preferred precipitating agents in accordance with the present invention.
The use of Ca(DTC).sub.2 has been found to have beneficial effects on flocculation and clarification because it decreases sludge production. The calcium dimethyldithiocarbamate salt also avoids problems with sodium limits in areas where the production of sodium containing species are regulated.
Additionally, the calcium salt, as opposed to other group II metal dimethyldithiocarbamates, has been found to precipitate out sulfates and fluorides and to cancel the chelating function of ethylenediaminetetraacetic acid (EDTA) which may be present in the waste water. This beneficial precipitating function of calcium dimethyldithiocarbamate is believed to be brought about by the relatively strong basicity of the Ca.sup.++ cation. Further, although a more dense sludge is formed, calcium dimethyldithiocarbamate has been found to produce a decreased sludge volume.
When the DTC precipitating agent employed is calcium dimethyldithiocarbamate, the following generalized reaction takes place:
where the heavy metal chelated may be any heavy metal with copper being used for illustration only.
Additionally, as noted above, the calcium salt has been found to displace the EDTA ligand from the heavy metal such that, generally speaking:
thereby precipitating the copper or other heavy metal from solution.
These and other modifications and variations to the present invention may be practiced by those of ordinary skill in the art, without departing from the spirit and scope of the present invention, which is more particularly set forth in the appended claims. Furthermore, those of ordinary skill in the art will appreciate that the foregoing description is by way of example only, and is not intended to be limitive of the invention so further described in such appended claims.
Claims
What is claimed is:
1. A method of waste water treatment, comprising: conducting pH treatment of a controlled body of waste water for substantially precipitating non-chelated and non-complexed metals therefrom; sampling such pH-treated waste water, and substantially removing solid precipitated metals therefrom to provide a clear sample; testing such clear sample for the presence of any remaining metals in solution therein; and feeding a group II metal dithiocarbamate to the controlled body of waste water in response to the presence of such remaining metals so as to substantially precipitate same, whereby both pH-precipitated and non-pH-precipitated metals are substantially precipitated from such body of waste water for removal therefrom, with minimized feeding of said group II metal dithiocarbamate.
2. A method as in claim 1, wherein said group II metal dithiocarbamate is a calcium dithiocarbamate.
3. A method as in claim 2, wherein said calcium dithiocarbamate is calcium dimethyldithiocarbamate.
4. A process of removing heavy metals from waste water, said process including the steps of: continuously sampling the waste water and removing from such sampling already precipitated metals so as to provide a clear sample; injecting a group II metal dithiocarbamate into such clear sample so as to render same turbid to a degree determined by the reactionary precipitation of metals formerly remaining in solution in such clear sample; detecting the degree of turbidity of such injected sample, so as to ascertain a proportional corresponding degree to which metals remain in solution in the waste water; and providing a regulated flow of said group II metal dithiocarbamate to the waste water in correspondence with the ascertained degree to which metals remain in solution in such waste water, whereby such regulated flow enables precipitation of heavy metals from the waste water substantially without over-feed of the group II metal dithiocarbamate, which minimizes sludge production accompanying use of such group II metal dithiocarbamate.
5. A process as in claim 4, wherein: said sampling and removing steps include establishing a sample flow from the waste water through filter means for filtering precipitants therefrom larger than a predetermined size; said injecting step includes injecting a relatively diluted strength of said group II metal dithiocarbamate into said sample flow; and said process further includes the step of returning said sample flow to the waste water, after performance of said injecting and detecting steps thereon.
6. A process as in claim 5, wherein: the waste water from which said sample flow is established also undergoes pH-treatment for substantially precipitating non-chelated and non-complexed metals therefrom, which are removed during said removing step; and said process further includes the step of periodically backwashing said filter means with reverse flow therethrough so as to prevent clogging thereof with such pH-treatment precipitated non-chelated and non-complexed metals, whereby relatively continuous operation of said process is afforded.
7. A process as in claim 4, wherein said providing step includes set-point control of said regulated flow, so as to permit flow of said group II metal dithiocarbamate only whenever the degree of turbidity is detected as being above a predetermined set-point.
8. A process as in claim 4, wherein said providing step includes modulated control of said regulated flow, so as to provide flow of said group II metal dithiocarbamate in proportion with the detected degree of turbidity.
9. A waste water treatment process for reducing metals in solution with such waste water to a predetermined level, said process including: providing multiple treatment stages for waste water including at least one stage constituting a main treatment tank having inflow thereto and outflow therefrom relative other treatment stages in the process; controlling the pH level in said main treatment tank so as to precipitate those metals therefrom amenable to pH-induced precipitation at the controlled level of such pH; continuously monitoring said main treatment tank for remaining non-precipitated metals; and based on such monitoring, selectively administering calcium dimethyldithiocarbamate to said main treatment tank for precipitating such remaining metals to a degree adequate to reduce metals in solution with such waste water to said predetermined level; wherein said monitoring and administering steps include: establishing a continuous sample flow from said main treatment tank, filtering said continuous sample flow to remove precipitated metals therefrom so as to provide a relatively clear continuous sample flow, continuously injecting a relatively diluted amount of calcium dimethyldithiocarbamate into said relatively clear continuous sample flow at an injection point in such flow, detecting the turbidity of such flow at a point downstream from said injection point, the degree of such turbidity varying in proportion with the degree to which additional metals are precipitated by said injecting of the diluted calcium dimethyldithiocarbamate, and actuating said administering of calcium dimethyldithiocarbamate to the main treatment tank responsive to the degree of detected turbidity, whereby such administering of calcium dimethyldithiocarbamate is in accordance with a monitored need for additional precipitation measures other than said pH level control, which minimizes sludge production inherently generated by use of a dithiocarbamate precipitating agent.
10. A process as in claim 9, wherein: said continuous sample flow from said main treatment tank is established at a relatively low flow rate; and said process further includes a preliminary equalization stage situated upstream from said main treatment tank and providing said inflow thereto; and said process further includes treatment stages situated downstream from said main treatment tank and receiving said outflow therefrom, such downstream stages consecutively including coagulation, flocculation, and clarification stages.
11. A process as in claim 9, wherein: said predetermined level of metals in solution with the waste water is generally in a range of from about zero to about 5 parts per million; said continuous sample flow from said main treatment tank has a flow rate generally within a range of from about 1 to about 20 gallons per minute; said filtering of said continuous sample flow includes filtering with membranes having a minimum particle trapping size generally in a range of from about 0.2 microns to about 5 microns; said pH-level control includes controlling such pH level in said main treatment tank to generally within a range of from about 4 to about 12; and said metals amenable to pH-induced precipitation are generally non-heavy metals, while said remaining non-precipitated metals are generally heavy metals which are chelated and/or complexed.
12. A process as in claim 9, wherein: said pH-level control includes maintaining the level of said pH in said main treatment tank generally below 4; and preliminary treatment stages of said process upstream from said main treatment tank include an equalization stage followed by a flocculation stage.
13. A process as in claim 9, wherein: said filtering step includes providing a pair of tubular filters, interconnected with controllable valves for directed flow therethrough in a selected longitudinal direction; and said waste water treatment process further includes the step of controlling said valves so as to intermittently reverse the longitudinal flow direction within said filters, and/or admit reverse flow direction water thereto from a clean external source, for backwashing same, whereby substantially continuous monitoring and administering may take place.
14. A process as in claim 9, wherein said administering actuating is based on set point control so that only degrees of detected turbidity above a predetermined set point actuate administering of calcium dimethyldithiocarbamate to the main treatment tank.
15. A process as in claim 9, wherein said actuating step includes modulated administering of calcium dimethyldithiocarbamate to the main treatment tank proportionately responsive to the degree of detected turbidity, for proportionately administering calcium dimethyldithiocarbamate in accordance with said monitored need therefor.
16. Apparatus for waste water treatment, comprising: pH treatment means for conducting pH treatment of a controlled body of waste water for substantially precipitating non-chelated and non-complexed metals therefrom; sampling means for sampling said pH treated waste water; separation means for substantially removing solid precipitated metals from said sampled pH treated waste water to provide a clear sample; testing means for testing said clear sample for the presence of any remaining metals in solution therein; and feeding means for feeding a group II metal dithiocarbamate precipitating agent to the controlled body of waste water in response to the presence of said remaining metals so as to substantially precipitate same, whereby both pH-precipitated and non-pH-precipitated metals are substantially precipitated from such body of waste water for removal therefrom, with minimized feeding of said group II metal dithiocarbamate precipitating agent.
17. Apparatus as in claim 16, wherein said group II metal dithiocarbamate precipitating agent is calcium dithiocarbamate.
18. Apparatus as in claim 17, wherein said calcium dithiocarbamate is calcium dimethyldithiocarbamate.
19. Apparatus for removing heavy metals from waste water, comprising: sampling means for continuously sampling such waste water; separation means for removing from such sampling already precipitated metals so as to provide a clear sample; injection means for injecting a calcium dithiocarbamate precipitating agent into said clear sample so as to render same turbid to a degree determined by the reactionary precipitation of metals formerly remaining in solution in said clear sample; turbidity detection means for detecting the degree of turbidity of said injected sample, so as to ascertain a proportional corresponding degree to which metals remain in solution in the waste water; and precipitating agent flow control means, responsive to said turbidity detection means, for providing a regulated flow of said calcium dithiocarbamate precipitating agent to the waste water in correspondence with the ascertained degree to which metals remain in solution in such waste water, whereby such regulated flow enables precipitation of heavy metals from the waste water substantially without overfeed of said calcium dithiocarbamate precipitating agent, which minimizes sludge production accompanying use of such agent.
20. Apparatus as in claim 19, wherein said calcium dithiocarbamate precipitating agent is calcium dimethyldithiocarbamate.
21. Apparatus as in claim 20, wherein: said sampling means includes tubing means for establishing a sample flow from the waste water; said separation means includes filter means for filtering from said sample flow of waste water precipitants larger than a predetermined size, which flow is directed therethrough by said tubing means; said injection means includes injection pump means for injecting a relatively diluted strength of calcium dimethyldithiocarbamate into said sample flow; and wherein said apparatus further comprises return flow means for returning said sample flow to the waster water, after operation of said injection means and turbidity detection means thereon.
22. Apparatus as in claim 21, further comprising: pH-level treatment means for substantially precipitating non-chelated and non-complexed metals from the waste water from which said sample flow is established with said tubing means, which precipitated metals are substantially removed from such sample flow by said filter means; and backwashing means for periodically backwashing said filter means with reverse flow therethrough so as to prevent clogging thereof with such pH-treatment precipitated non-chelated and non-complexed metals, so as to permit relatively prolonged periods of operation of said filter means without other substantial maintenance thereof.
23. Apparatus as in claim 20, wherein said precipitating agent flow control means includes set-point control means for permitting flow of calcium dimethyldithiocarbamate only whenever the degree of turbidity detected by said turbidity detection means is above a predetermined set-point.
24. Apparatus as in claim 20, wherein said precipitating agent flow control means includes modulated control means for providing controlled flow of calcium dimethyldithiocarbamate in proportion with the detected degree of turbidity determined by said turbidity detection means.
25. A waste water treatment system for reducing metals in solution with such waste water to a predetermined level, said system including: a plurality of consecutive treatment stages for waste water including at least one stage constituting a main treatment tank having inflow thereto and outflow therefrom relative other treatment stages in said system; pH-level control means for controlling the pH level in said main treatment tank so as to precipitate those metals therefrom amenable to pH-induced precipitation at the controlled level of such pH; testing means for continuously monitoring said main treatment tank for remaining non-precipitated metals; and control means, responsive to said testing means, for selectively administering calcium dimethyldithiocarbamate to said main treatment tank for precipitating such remaining metals to a degree adequate to reduce metals in solution with such waste water to said predetermined level; wherein said testing means and control means include tubing means for establishing a continuous sample flow from said main treatment tank, liquid-solid separation means for filtering said continuous sample flow to remove precipitated metals therefrom so as to provide a relatively clear continuous sample flow, precipitating agent injection pump means for continuously injecting a relatively diluted amount of calcium dimethyldithiocarbamate into said relatively clear continuous sample flow at an injection point in said flow, turbidity meter means for detecting the turbidity of said flow at a point downstream from said injection point, the degree to such turbidity varying in proportion with the degree to which additional metals are precipitated by said injecting of said diluted calcium dimethyldithiocarbamate, and precipitating agent controlled pump means, responsive to said turbidity meter means, for pumping calcium dimethyldithiocarbamate to said main treatment tank responsive to the degree of detected turbidity, whereby such controlled pumping of calcium dimethyldithiocarbamate is in accordance with the detected need for additional precipitation measures other than said pH level control, which minimizes sludge production inherently generated by use of calcium dimethyldithiocarbamate.
26. A system as in claim 25, wherein: said tubing means comprises relatively small diameter tubing for establishing a relatively low flow rate continuous sample flow; and wherein said system further includes a preliminary equalization stage situated upstream from said main treatment tank and providing said inflow thereto; and treatment stages situated downstream from said main treatment tank and receiving said outflow therefrom, such downstream stages consecutively including coagulation, flocculation, and clarification stages.
27. A system as in claim 25, wherein: said pH-level control means is operative for maintaining the level of said pH in said main treatment tank generally below 4; and said other treatment stages of said system include upstream from said main treatment tank an equalization stage followed by a flocculation stage.
28. A system as in claim 25, wherein: said separation means includes a pair of tubular filters, interconnected with a plurality of controllable valves for directed flow therethrough of said continuous sample flow in a selected longitudinal direction of said tubular filters; and said control means further includes means for controlling operation of said valves so as to intermittently reverse the longitudinal flow direction within said tubular filters, and/or admit reverse flow direction water thereto from a clean external source, for backwashing said tubular filters.
29. A system as in claim 25, wherein said control means includes set point control means for operating said precipitating agent controlled pump means so that only degrees of detected turbidity above a predetermined set point actuates feeding of calcium dimethyldithiocarbamate to said main treatment tank.
30. A system as in claim 25, wherein said control means includes modulation means for operating said precipitating agent controlled pump means so that actuation thereof is modulated proportionately to the degree of detected turbidity, for proportionately actuating feeding of calcium dimethyldithiocarbamate to said main treatment tank in accordance with said detected need therefor.
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