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Water Conservation In Pulp & Paper Industry Through Innovative Water Management & Modeling Techniques. R. M. Mathur, B.P. Thapliyal, A.K. Goel. Central Pulp And Paper Research Institute P.O.Box. 174, Saharanpur. Pulp and paper industry is one of the major water consuming industries.
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Water Conservation In Pulp & Paper Industry Through Innovative Water Management & Modeling Techniques. R. M. Mathur, B.P. Thapliyal, A.K. Goel Central Pulp And Paper Research Institute P.O.Box. 174, Saharanpur
Pulp and paper industry is one of the major water consuming industries. • Water is used for a variety of processes and gets contaminated during processing with raw materials,chemicals, by-products & residues. • Treatment of contaminated wastewater has always been an expensive & technically challenging subject.
Water management techniques can prove to be highly effective as they enable efficient usage of water with considerations of • reuse, • recycle and • regeneration opportunities.
Process Integration The application of methodologies aimed at designing/modernizing an Industrial Facility by optimizing its various constituent units rather than improving each individual unit by itself.
Process Integration Methods • Classical pinch based • Mathematical programming based
Pinch Based Approach • Graphical technique to minimize fresh water flow • An extension of the pinch analysis technique for heat integration. • Water surplus diagrams are utilized to target water requirement.
Purity Fresh Water Water Sources Concentration Water Demands Water Pinch Waste water Water Flow Water Pinch – Composite Curves • Each water related process operation considered as having water inputs and output streams and composite of water demand (Input) and water sources (Output) can be constructed. • Not suitable for multiple contaminant systems
Mathematical Programming Approach • The pinch point ( pinch concentration and pinch mass load) is calculated by application of Composite Table Algorithm (CTA). • A system of equations is solved with constraints to get values for various water streams. • A Network is generated by applying Nearest Neighbor Algorithm (NNA) • Network of all possible matches is created and the system is optimized for minimum fresh water requirement based on capital/operating expenses.
Advantages of Mathematical Programming Approach • Provides a robust way of water network design. • Provides insight into water targeting with a consideration of recycle, reuse & regeneration.
Basic Network Structure • A basic integrated water network consists of a set of water using and water treating operations. • Each water using operation demands a certain quality and quantity of water to satisfy its process needs. • This demand may be fulfilled by mixing fresh water with effluent streams from other water using operations and regenerated water. • The process outlet streams may be used to satisfy the demand of other operations, sent to treatment units or discharged without treatment.
C P in C P out Process C Water out C Water in C P in C W out Concetration C P out C W in m, Mass flow rate Unit operation mass flow
Process 4 800 Concetration Process 3 400 Water Supply Line 100 Process 1& 2 m, Mass flow rate m, Mass flow rate Water limiting profile Limiting Profile curve
CASE STUDY • Mill Details:- • Production 75,000tpa • Products - Printing and writing papers • Raw materials - hardwood and bamboo , ratio(84:16) • 6 paper machines • 3 stationary batch digesters • Pulp is bleached by using C/DEopD1D2 bleaching sequence.
METHODOLOGY • The study was carried out for two contaminants (TS & COD) in the bleach plant for reuse & recycle options. • A complete water balance of the pulp mills was prepared using online & portable flow meters. • The water samples from various streams were characterized with respect to their pollution load.
Water Balance Flow Diagram for Mill ( All Figures in m3/hr)
Data Extraction: • All operations assumed to be fixed contaminant (FC) and fixed flowrate operations type. The limiting contaminant levels are fixed at 10 % above the current values. • Restriction on re use of water streams • All matches prohibited by pH are disallowed. • Order and flowrate from one process to another is maintained
368 368 S 1 CD D 1 1854 2970 Pulp washing 403 403 EOP S 2 D 2 Pulp washing 1190 2081 367 367 D1 S 3 D 3 Pulp washing 1037 1910 373 373 D2 S 4 D 4 Pulp washing 990 1447 847 847 Decker S 5 D 5 Pulp washing 656 656 Fig. Extracted Flow Diagram
Flow = FlowDemand - FlowSource Flow x ( C2 – C1)/1000 ………..m……... C - Cmin Pinch conc. Pinch Load Pinch point Composite Table Algorithm
3000 2500 2000 1500 1000 500 0 250 500 750 1000 1250 1500 Limiting Composite Curve Water Composite curve Pinch Line Pinch Concentration Contaminant Concentration, ppm Limiting Composite Curve Pinch Load Contaminant Load, kg/hr
Nearest Neighbour Algorithm • Sources which are immediate higher/ lower in concentration for a demand are mixed in ratio determined by mass balance to satisfy the demand. • If the required flow rate is not available for a source, than whatever is available of that source is used completely & next neighbor is considered to satisfy the demand.
Nearest Neighbour Algorithm The mass balance equations are- FSK, DP + FS(K+1),DP = FDP FSK, Dp CSK +FS(K+1),DP CS(K+1) =FDP CDP Where F&C are flowrate & concentration SK & S(K+1) are immediate cleaner& dirtier sources ( Nearest Neighbour) DP is the particular demand.
Conclusion • The study conducted in selected mills in the pulp mill section has shown that PI studies can be a valuable tool for water conservation. • Application of the mathematical programming model developed for water minimization has shown scope of water savings in both the mills after selecting suitable water networks.