FLUIDIZED BED PELLET REACTOR WATER SOFTENER AND PROCESS FOR SOFTENING WATER

Abstract

As pellets grow from seed/sand in a fluidized bed pellent reactor, the weight of the reactor is measured and the density of the contents of the reactor is calculated, and the input flow of untreated water, water treatment chemical, and seed/sand are adjusted to provide improved removal of water hardness while reducing fine particulates in the outflow of softened water from the reactor.

Claims

1. A process for softening water, the process comprising: providing a fluidized bed pellet reactor for softening hard water, the reactor comprising: a seed storage tank for storing fine sand for use as crystallization seeds, a reactor tank for containing a fluidized bed of pellets, an inflow pump for pumping inflow fluid to be treated into the reactor tank to fluidize the bed of pellets, a reagent storage tank for storing a chemical reagent for adjusting the pH of the fluid in the reactor tank, means for delivering seed from the seed storage tank to the reactor tank, means for delivering reagent from the reagent storage tank to the reactor tank, means for withdrawing pellets from the reactor tank, and means for measuring the weight of the reactor tank and the contents of the reactor tank; the process further comprising: mixing a predetermined weight of seed with a predetermined volume or weight of water in the seed storage tank to form a mixture of seed and water; filling the reactor tank with a predetermined volume of water; transferring a predetermined amount of the mixture of seed and water from the seed storage tank to the reactor tank; pumping inflow liquid including calcium ion to be treated into the reactor tank to create a fluidized bed; delivering reagent from the reagent storage tank to the reactor tank to crystallize the calcium ion as calcium carbonate on the seed to form pellets; maintaining the density of the fluidized bed at a predetermined optimum density; withdrawing treated water as an effluent from the reactor tank; withdrawing pellets from the reactor tank.

2. A process according to claim 1 wherein the speed of the inflow pump is controlled to maintain the predetermined density.

3. A process according to claim 1 further comprising: providing means for measuring the weight of the seed storage tank and the contents of the seed storage tank.

4. A process according to claim 1 further comprising providing a hopper for receiving pellets from the reactor, the hopper including means for measuring the weight of the hopper, and permitting gravity dewatering of the pellets received from the reactor, and monitoring the loss of weight of the pellets as the pellets are dewatered.

5. A process according to claim 1 wherein the means for measuring the weight of the reactor tank includes a plurality of load cells for sensing the distribution of weight within the reactor tank, the process further comprising sensing the distribution of weight of the contents of the reactor tank and comparing the sensed distribution of weight with a predetermined distribution.

6. A process according to claim 3, the process further comprising: delivering seed sand to the seed storage tank, determining the weight of the seed sand in the storage tank; delivering water to the seed storage tank; measuring the weight of the water in the storage tank, wherein the water and sand are delivered in quantities sufficient to achieve a predetermined ratio of sand to water.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0014] FIG. 1 is a schematic representation of a fluidized bed pellet reactor of the prior art.

[0015] FIG. 2 is a schematic representation of a fluidized bed pellet reactor of the present invention.

[0016] FIG. 3 is a fragmentary schematic bottom plan view of a reactor tank according to one presently preferred aspect of the present invention.

[0017] FIG. 4 is a schematic elevational view of a sand cleaning subsystem for preparing seed for use in the present invention.

DETAILED DESCRIPTION

[0018] Referring now to the figures in which like reference numerals represent like elements in each of the several views, there is shown in FIG. 1, a schematic representation of a fluidized bed pellet reactor 10 of the prior art, commonly referred to as an “Amsterdam” reactor. An influx flow 12 of water to be treated is pumped into the bottom of a generally vertical reactor tank 14. The water flows upward in the tank 14 in the direction shown by the arrows. At the same time, a basic reagent 16 such as sodium hydroxide or sodium carbonate is pumped into the bottom of the tank 14 and dispersed in the upward flow of the influx water. Seed or fine sand 22 is admitted into the tank 14 and is suspended in the tank 14 by the upward flow of the water in the tank 14, forming a fluidized bed. Calcium ions dissolved in the upflowing, basic, water precipitate or crystallize on the seeds, thus removing dissolved calcium to “soften” the water and forming pellets The softened water, or treated effluent 24, is discharged from the upper portion of the tank 14. Periodically, the largest pellets, which tend to settle to the bottom of the tank 14, are discharged 18 from the reactor 10 and recycled for industrial or agricultural purposes.

[0019] FIG. 2 is a schematic representation of fluidized bed pellet reactor 100 of the present invention for carrying out the process of the present invention. The pellet reactor 100 includes a generally vertical reactor tank 102 for containing the fluidized bed 116. The flow of influent water 112 to be treated is provided near the bottom of the tank 102 by an influent pump 132 from calcium ion containing water 130 delivered from an external source. A chemical reagent or reactant such as sodium hydroxide or sodium carbonate is stored in a reagent storage tank 140 and delivered to the reactor tank 102 near the bottom thereof by suitable means such as by reagent metering or dosing pump 142. Seed or fine sand mixed with water is stored in a seed storage tank 150 and the mixture is delivered 120 to the reactor tank 102 at a predetermined elevation above the bottom of the reactor tank 102. Seed inflow 120 is controlled by suitable means 152, such as by a valve, a metering or dosing pump, or by some combination thereof. As the seed enters the basic upward flow of the calcium ion containing water to be treated, calcium carbonate precipitates or crystallizes on the surface of the seed, forming pellets composed largely of calcium carbonate. The pellets so formed are periodically discharged 118 from the bottom of the reactor tank 102 and stored in a pellet hopper 160 where water 250 is permitted to drain from the wet pellets. Pellet removal is controlled by suitable means 162, such as by a valve or pump, or a combination of the two. Treated effluent 122 is discharged from the upper end of the reactor tank 102 through an outflow pipe, outflow valve, or other suitable means. A baffle 124 is provided at or near the upper end or top of the reactor tank to limit the surface area of the top of the reactor tank 102 so as to limit the rise rate of the fluidized bed 116 in the reactor tank 102. Preferably, a device 260 for sensing the height of the fluidized bed 116 in the reactor tank 102 is provided, such as an acoustic, magnetostrictive or like device.

[0020] Operation of the pellet reactor 100 is preferably controlled by a central controller, which can be a specialized controller or a general purpose computer 200. The reactor tank 102 is provided by one or more load cells 210 which are connected to the computer 200 by one or more suitable sensing lines 222, such that the weight of the reactor tank 102 can be monitored continuously as the reactor tank 102 is filled with influent 112, reagent 114, and seed 120, and as pellets are formed on the seed, thus permitting the weight/or and density of the fluidized bed 116 within the reactor to be monitored. Preferably, the turbidity and/or total hardness of the effluent are also monitored (not shown), so that the input parameters, the input pump speed, rate of reagent addition, and rate and quantity of seed addition can be adjusted to provide a desired level of hardness reduction while minimizing release of particulate fines in the effluent which must be subsequently removed, such as by filtration.

[0021] The height of the fluidized bed 116 in the reactor tank 102 can be monitored and measured by a scale of suitable means, for example, acoustically. The average density of the fluidized bed 116 can be calculated based upon weight and volume.

[0022] The inflow pump 132 can be controlled by the computer 200 through a suitable control line. The speed of the inflow pump 132 can be varied and/or a valve can be used to adjust the pumping rate (not shown).

[0023] The computer 200 can optionally monitor the weight of the seed storage tank 150 by suitable means such as one or more load cells 214 through a suitable sensor line 218. Thus, seed storage tank 150 can be tared, and as water and seed/sand are sequentially added to the seed storage tank 150, the weight ratio of the two can be calculated, and the amount of seed/sand/water 120 delivered to the reactor tank 102 can be monitored.

[0024] The computer 200 can optionally also monitor the weight of the reagent storage tank 140 (and thus the weight of the reagent) by suitable means such as by one or more load cells 212 and corresponding sensing line 224, and control operation of the means for delivering reagent 142 (i.e. the valve or metering pump) to the reactor tank 102 through a suitable control line 226. Thus, the rate at which reactant 114 is delivered to the reactor tank 102 can be optimized to maximize the removal of dissolved calcium from the influent water 112.

[0025] Examples of reagents that can be employed in the process of the present invention include Ca(OH).sub.2 slurry; quicklime, hydrated lime, sodium hydroxide, soda ash, calcium sulfate, lime-soda ash, and caustic soda. In addition, sundry additives can be includes, and the seed bed or a portion of the seed bed can be recirculated.

[0026] In addition, the weight of the pellet hopper 160 is sensed by one or more load cells 216 and then provided to the computer 200 through sensor line 228. After wet pellets have been discharged from the reactor tank 102, drying of the pellets can be monitored as the sensed weight of the pellets declines as water 250 drains from the pellet hopper 160, and the dried pellets 252 can be thus discharged from the pellet hopper 160 when a predetermined level of dryness has been obtained. Discharge of pellets from the reactor tank 102 can be controlled by any suitable means, such as by a valve 162. Operation of the valve 162 can be controlled by the computer 200 through a control line 232. The dried pellets can be transferred, for example, by a conveyor, to storage bins, for later transfer to trucks, for example. The pellets can be processed, stored in storage bins, and discarched into trucks for remote transport, such as disclosed, for example, in U.S. Pat. Nos. 6,698,766, and 8,682,477, the entire disclosures of which are incorporated herein by reference.

[0027] In another presently preferred embodiment of the present invention, a plurality of load cells 210, 212, 214, 216 (FIG. 3) are provided under the supporting legs of the reactor tank 102, so that the distribution of the weight of the fluidized bed 116 in the reactor tank 102 can be monitored, and a distribution deviating from uniform can be corrected.

[0028] Seed sand for use in the process of the present invention can be prepared using a suitable subsystem 400, such as illustrated in FIG. 4. In the process and apparatus of the subsystem 400, sand which may have various contaminants, is transferred from a suitable store (not shown) by a conveyor 402 equipped with load cells 404 for measuring the weight of sand being transported by the conveyor 402, and delivered to a hopper 406, which is supported by a plurality of legs 408, and which are also provided with load cells 410 for monitoring the weight of sand delivered to be washed. Sand is discharged through a flow-control valve 414 to an agitator or agitation tank 430, which is supplied proximate the bottom of the agitation tank 430 with clean wash water 434 through a modulating valve 438 for controlling the rate of flow of the clean water into the tank. The rate of flow of clean water into the agitation tank 430 is monitored with a flow meter 436. As the clean water flows upwards through sand in the agitation tank 430, impurities are removed, and the resulting dirty water is removed through an outlet 420 at the top of the agitation tank 430. As need be, clean water 412 can be supplied to the agitation tank 430 near the top of the agitation tank 430 to clean the agitation tank 430, and the resulting dirty water can be discharged through a tank drain 450 at the bottom of the tank. Clean seed sand 440 can be discharged through a valve near the bottom of the agitation tank 430.

[0029] Various modifications can be made in the details of the various embodiments of the apparatus and process of the present invention, all within the scope and spirit of the invention and defined by the appended claims.