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PROCESS CONTROLLER FOR TREATING WASTE OILS IN AUTOMOTIVE WASTE TREATMENT PLANTS Sanjay R. Srivatsa, Senior Research Engineer E. C. Zuerner, Group Leader Nalco Chemical Company Naperville, Illinois 60566 INTRODUCTION Heretofore, batch cooking processes are generally implemented in the recovery of oil from waste oil scum. These processes consist of heating the waste oil scum followed by addition of emulsion breaking chemicals to produce an oil-water resolution. Waste oil scums are water-in-oil emulsions generated in processes utilizing water, oil, cleaners, etc., in the machining and working of metals. Automotive industries comprise the major source for waste oil scum. Other sources are refineries, steel-rolling mills, canning industries, chemical processing and hydrocarbon processing industries. Because of the ever increasing value of oil and the economics of a waste oil recovery program, it is worthwhile to maximize oil recovery from these waste emulsions for reuse. Waste oil emulsions consist of three components, namely, oil, water, and solids. The conventional method of breaking down the waste emulsion is as follows: 1. Addition of acid/caustic, 2. Heating the cooker to a desired temperature, 3. Mixing in a proportion of an organic (synthetic) emulsion breaker, 4. Allowing the contents to resolve into oil and water. Heating incorporates the primary step in the resolution of a waste oil emulsion. A resolved emulsion consists of three discrete phases, namely, oil, water, and an unresolved intermediate phase called rag. This phase consists of undissolved solids held in a tight matrix of water-in-oil. The rag has to be retreated in order to further resolve this phase. This results in higher chemical demand and special handling procedures. Thus, the generation of rag has to be minimized to ensure smooth operation and curtail recurring energy and chemical costs. Major factors controlling the generation of rag are chemical dose and agitation. Inadequate or excessive chemical dosage can result in a large volume of rag. The effect of agitation is analogous to chemical dose in that overmixing can cause reemulsification of resolved water and oil, thus, minimizing oil recovery. Due to constant variations in the waste oil source, every batch justifies a specific chemical dosage for minimizing rag and enhancing oil recovery. Current dosage control procedures call for conducting 50 ml, bottle tests where chemicals are titrated into the sample and optimized qualitatively (visually). These tests take between 4-12 hours to predict optimum dosages. As batches are treated continuously, this procedure is not practiced by shift operators on a regular basis. Furthermore, the test offers merely a crude scale-up (50 mis to 4,000-10,000 gallons) leading to poor simulation of heat transfer and hydraulics. Thus, a high percentage of cooker resolutions tend to be dissimilar to that of bottle tests. As a result, conventional cooker dosages are limited to a fixed level of acid/caustic and emulsion breaker. The dosages are determined once, thereafter, all subsequent batches are treated similarly. Evidently, the outcome of this procedure is an overall reduction in oil recovery due to poor batchwise optimization. In addition to this, a considerable number of batches have to be rescheduled to treat large quantities of rag consuming additional energy, chemicals, and process time. This paper addresses the development of a revolutionary on-line technique for optimizing chemical feed and energy requirements in automotive waste oil cookers. Case histories illustrate the success of this technique in its capacity to maximize yields and improve process economics. 27
Object Description
Purdue Identification Number | ETRIWC198405 |
Title | Process controller for treating waste oils in automotive waste treatment plant |
Author |
Srivatsa, Sanjay R. Zuerner, E. C. |
Date of Original | 1984 |
Conference Title | Proceedings of the 39th Industrial Waste Conference |
Extent of Original | p. 27-36 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital object copyright Purdue University. All rights reserved. |
Language | eng |
Type (DCMI) | text |
Format | JP2 |
Date Digitized | 2009-07-16 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 27 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital copyright Purdue University. All rights reserved. |
Language | eng |
Type (DCMI) | text |
Format | JP2 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Transcript | PROCESS CONTROLLER FOR TREATING WASTE OILS IN AUTOMOTIVE WASTE TREATMENT PLANTS Sanjay R. Srivatsa, Senior Research Engineer E. C. Zuerner, Group Leader Nalco Chemical Company Naperville, Illinois 60566 INTRODUCTION Heretofore, batch cooking processes are generally implemented in the recovery of oil from waste oil scum. These processes consist of heating the waste oil scum followed by addition of emulsion breaking chemicals to produce an oil-water resolution. Waste oil scums are water-in-oil emulsions generated in processes utilizing water, oil, cleaners, etc., in the machining and working of metals. Automotive industries comprise the major source for waste oil scum. Other sources are refineries, steel-rolling mills, canning industries, chemical processing and hydrocarbon processing industries. Because of the ever increasing value of oil and the economics of a waste oil recovery program, it is worthwhile to maximize oil recovery from these waste emulsions for reuse. Waste oil emulsions consist of three components, namely, oil, water, and solids. The conventional method of breaking down the waste emulsion is as follows: 1. Addition of acid/caustic, 2. Heating the cooker to a desired temperature, 3. Mixing in a proportion of an organic (synthetic) emulsion breaker, 4. Allowing the contents to resolve into oil and water. Heating incorporates the primary step in the resolution of a waste oil emulsion. A resolved emulsion consists of three discrete phases, namely, oil, water, and an unresolved intermediate phase called rag. This phase consists of undissolved solids held in a tight matrix of water-in-oil. The rag has to be retreated in order to further resolve this phase. This results in higher chemical demand and special handling procedures. Thus, the generation of rag has to be minimized to ensure smooth operation and curtail recurring energy and chemical costs. Major factors controlling the generation of rag are chemical dose and agitation. Inadequate or excessive chemical dosage can result in a large volume of rag. The effect of agitation is analogous to chemical dose in that overmixing can cause reemulsification of resolved water and oil, thus, minimizing oil recovery. Due to constant variations in the waste oil source, every batch justifies a specific chemical dosage for minimizing rag and enhancing oil recovery. Current dosage control procedures call for conducting 50 ml, bottle tests where chemicals are titrated into the sample and optimized qualitatively (visually). These tests take between 4-12 hours to predict optimum dosages. As batches are treated continuously, this procedure is not practiced by shift operators on a regular basis. Furthermore, the test offers merely a crude scale-up (50 mis to 4,000-10,000 gallons) leading to poor simulation of heat transfer and hydraulics. Thus, a high percentage of cooker resolutions tend to be dissimilar to that of bottle tests. As a result, conventional cooker dosages are limited to a fixed level of acid/caustic and emulsion breaker. The dosages are determined once, thereafter, all subsequent batches are treated similarly. Evidently, the outcome of this procedure is an overall reduction in oil recovery due to poor batchwise optimization. In addition to this, a considerable number of batches have to be rescheduled to treat large quantities of rag consuming additional energy, chemicals, and process time. This paper addresses the development of a revolutionary on-line technique for optimizing chemical feed and energy requirements in automotive waste oil cookers. Case histories illustrate the success of this technique in its capacity to maximize yields and improve process economics. 27 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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