Bombas de Lodos
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BOMBAS DE LODOS
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BOMBAS DE SLURRY – GOULDS PUMPS Curso Básico de Bombas de Lodos Junio, 2012. Por Luis Lopez LIMA SALES OFFICE ITT GOULDS PUMPS
Objetivo Crear un lenguaje comun Proveedor – Usuario. Afirmar y/o clarificar conocimientos basicos de hidraúlica/bombas de lodos en su selección / aplicación / necesidades de equipos de bombeo / instalacion / mantenimiento / operacion / mejora-optimizacion y garantia Generar la identificacion de contactos/comunicacion Proveedor – Usuario.
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Reglas Celulares en modo vibración.
Alta concentración.
Preguntas en cualquier momento.
Respeto a sus compañeros.
Identificar rutas / zonas de seguridad. BOMBAS DE LODOS
De que hablaremos? 1. Introducción. 2. Conceptos básicos. 3. Cálculos básicos en Lodos. 4. Teoria de Funcionamiento. 5. Tipos de Bombas Goulds. 6. Desgaste en Bombas de Lodos. 7. Servicios Tipicos. 8. Materiales. 9. Criterios de Seleccion. Ejemplo. BOMBAS DE LODOS
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Introducción
Quienes somos?
ITT Goulds Pumps – Lima Sales Office Luis Carrasco
– Encargado de Oficina y Ventas Ecuador, Perú, Bolivia. Ghayle Mendoza – Encargado Logística, Ordenes. Fernando Meneses – Encargado Servicios Mejora Sistemas PPS LAR. Marcial Elías – Encargado Proyectos Perú, Ecuador, Bolivia. Gustavo Navarro – Encargado ProSmart, PumpSmart. Oscar Campos - Encargado Cuentas Ecuador. Edson Munoz - Encargado Cuenta Perú Sur, Bolivia. Luis López - Encargado Cuentas Perú Norte y Centro (Oil & Gas, Minería Norte y Centro, Industria). Rodrigo Flores - Encargado Propuestas de Perú. Willman Cortez - Encargado de Propuestas Perú Sur, Bolivia. Katerina Stumpfle - Estado de Ordenes, Ack. de Ordenes, facturas. Representantes - Perú Minería (Intech), Ecuador (La Llave Ecu) Bolivia (La Llave Bol, ETI). T:511-4756910, Fax 511-4757010. Av. Canaval y Moreyra 654, Piso 6, San Isidro, Lima, Perú. www.gouldspumps.com BOMBAS DE LODOS
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Introducción Por que son importantes las bombas centrífugas? 1. Representan el 45% de equipos usados en transporte de líquidos en “Procesos Continuos” en Plantas Industriales – PROCESO PRINCIPALES. Representan el 55% de equipos usados en transporte de líquidos en “Sistemas Auxiliares” en Plantas Industriales – PROCESO SECUNDARIOS. 2. Son la solución de transporte de fluidos más: Sencilla y Económica. 3. Representan el 20% del Consumo de energia elec. mundial. BOMBAS DE LODOS
LAS MAS USADAS, SENCILLAS Y ECONÓMICAS
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Introducción Por que son importantes las bombas centrífugas?
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Industrias que usan Bombas Centrifugas Markets Oil & Gas
General Industrial
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Power
Mining
Chemical
Pulp & Paper
ITT IP Global Presence
August 2007
ITT Goulds Pumps México. ITT Goulds Pumps Colombia. ITT Goulds Pumps Venezuela. ITT Goulds Pumps Perú. ITT Goulds Pumps Chile. ITT Goulds Pumps Brasil. ITT Goulds Pumps Argentina.
HIDRAULICA BASICA
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ITT Goulds Pumps Industrial Vertical Turbine & Propeller Pumps Applications: •High Volume Water Services for Cooling Towers, Power, Geothermal, General Industry , Municipal, API, Petroleum Refinery. Heavy Duty Process Pumps Applications: •Process Pumps In Hazardous Locations. Global API Standard.
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Goulds Standard Process Pumps ( ANSI & ISO Std.) Applications: •Medium & Heavy Duty End Suction Processes For Chemical, Paper & Mining, Water, Petrochemical, Hydrocarbon transfer. Water Services.
Product Overview Performance Solutions • PumpSmart® • ProSmart® • ProActivity
Chemical and Pulp & Paper Process • ANSI • ISO • MagDrive • Paper Stock
Slurry Process • Hard Metal • Rubber Lined General Service • Double Suction • Vertical Turbine • Sump
API Process • Overhung • Between Bearings • Multi-Stage Industrial Valves • Knife Gate • Diaphragm • Lined
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Monitoring and Control PumpSmart
Improving Plant Profitability
Integrated Pump Control, Protection, and Right-Sizing
Increased
UPTIME
Of your Process Decreased
MAINTENANCE
ProSmart Wireless Predictive Maintenance System
Activities
Decreased
ENERGY Costs
Performance Services Pump System Optimization Services
Goulds Pumps (Video)
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Desarrollo de la Primera Bomba de Lodos RL – Allis Chalmer 1921 Allis Chalmer pumps, tractor, crusher, mills manufacturer.
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Conceptos Básicos 2.1
Propiedades de los fluidos.
2.2
Viscosidad , Medicion de la Viscosidad.
2.3
Analisis Granulometrico
2.4
Tipos de flujo bifasico en tuberia.
2.5
Tip Speed y Desgaste BOMBA DE LODOS
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DO I NEED A SLURRY PUMP?
Just because the service is labeled slurry doesn’t always mean you need a slurry pump. Light slurries up to 5% solids or a 1.02 specific gravity may be pumpable with a process pump. Very important if higher metallurgy is required. Light slurries with sand may require a slurry pump. RPM as lower as possible. Is slurry application has froth factor?
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Conceptos básicos Propiedades de Fluidos Gravedad Específica, Densidad (Kg / m3) – Densidad Agua 1000 Kg/m3. Viscosidad. Aumenta, con el aumento de % solidos, al haber mayor presencia de arcilla. PH: Neutro = 7 , Acido < 7, Básico > 7. Temperatura. Regla Práctica, cada incremento de 20F aceleran al doble al ratio de corrosion. Contenido de Solidos: % En peso / Tamaño / Forma: Angular recomendable uso de Impeler de Metal. Componentes Corrosivos Agresivos. (Acidos, Sales, etc) Factor de Espuma.
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Fundamentos Densidad y Gravedad Especifica 1m
1 m3 En el Agua, 1m3 pesa 1000 Kg. y tiene una Gravedad Especifica GE de 1 En slurries, si 1m3 pesa 1200 Kg. y tiene una Gravedad Especifica GE de 1,20 BOMBAS DE LODOS
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Ns Definition
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Ns Impeller Type
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% Solidos vs Gravedad Especifica Sl
Sm
1.00
Cw% 30 Ss
2.70
Sm
1.23
Cv
13.6%
Ss
Cw%
Fundamentos de Slurries
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Fundamentos Concentración de Solidos
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Fundamentos Concentración de Solidos en peso, base acuosa
% Solidos vs Gravedad Especifica Sl 1.00 Cw% 30 Ss 2.70
Sm =
2.7 / ( 2.7+.3*(1-2.7))
Sm =
2.7 / ( 2.7+.3*(-1.7))
Sm =
2.7 / 2.19
Sm =
1.2328
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Fundamentos Concentración de Solidos en peso, base acuosa
% Solidos vs Gravedad Especifica Sl 1.00 Cw% 30 Ss 2.70
Sm =
1 / ( 1+.3*(1/2.7 - 1))
Sm =
1 / ( 1+.3*(-0.629629))
Sm =
1 / 0.811111
Sm =
1.2328
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Fundamentos Concentración de Solidos en peso, base acuosa
% Solidos vs Gravedad Especifica Sl 1.00 Cw% 40 Ss 2.70
Sm =
1 / ( 1+.4*(1/2.7 - 1))
Sm =
1 / ( 1+.4*(-0.629629))
Sm =
1 / 0.748148
Sm =
1.3366
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Fundamentos Concentración de Solidos en peso, base acuosa
% Solidos vs Gravedad Especifica Sl 1.00 Cw% 50 Ss 2.70
Sm =
1 / ( 1+.5*(1/2.7 - 1))
Sm =
1 / ( 1+.5*(-0.629629))
Sm =
1 / 0.685185
Sm =
1.4595
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Fundamentos Concentración de Solidos en peso, base acuosa
% Solidos vs Gravedad Especifica Sl 1.00 Cw% 60 Ss 2.70
Sm =
1 / ( 1+.6*(1/2.7 - 1))
Sm =
1 / ( 1+.6*(-0.629629))
Sm =
1 / 0.622222
Sm =
1.6071
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Fundamentos Concentración de Solidos en peso, base acuosa
% Solidos vs Gravedad Especifica Sl 1.00 Cw% 70 Ss 2.70
Sm =
1 / ( 1+.7*(1/2.7 - 1))
Sm =
1 / ( 1+.7*(-0.629629))
Sm =
1 / 0.559259
Sm =
1.7881
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Fundamentos Concentración de Solidos en volumen, base acuosa
% Solidos vs Gravedad Especifica Sl Cw% Ss Sm
1.00 30 2.70 1.2328
Cv =
30 * ( 1.2328 ) / (2.7)
Cv =
30 * ( 0.45659259 )
Cv = 13.698
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Fundamentos Concentración de Solidos en volumen, base acuosa
% Solidos vs Gravedad Especifica Sl Cw% Ss Sm
1.00 40 2.70 1.3366
Cv =
40 * ( 1.3366 ) / (2.7)
Cv =
40 * ( 0.495037 )
Cv = 19.801
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Fundamentos Concentración de Solidos en volumen, base acuosa
% Solidos vs Gravedad Especifica Sl Cw% Ss Sm
1.00 50 2.70 1.4595
Cv =
50 * ( 1.4595 ) / (2.7)
Cv =
50 * ( 0.540555 )
Cv = 27.028
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Fundamentos Concentración de Solidos en volumen, base acuosa
% Solidos vs Gravedad Especifica Sl Cw% Ss Sm
1.00 70 2.70 1.7881
Cv =
70 * ( 1.7881 ) / (2.7)
Cv =
70 * ( 0.662259 )
Cv = 46.358
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Fundamentos Concentración de Solidos en volumen, base acuosa
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Fundamentos Concentración de Solidos en base acuosa
Sm
Cw
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Fundamentos Concentración de Solidos
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Fundamentos Concentración de Solidos
Cw
Cv
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Concentración de Solidos % en Peso, % en Volumen
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Fundamentos Sm Gravedad Especifica del Lodo (Video)
Sl Cw% Ss Sm
1.00 74 3.4 2.09
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Fundamentos Caudal de Slurry
% Solidos vs Dry solids 2000 tons per day Gravedad Especifica Sl Cw% Ss Sm
1.00 30 2.70 1.2328
Qm = 4.4 * 2000 / (0.3 * 1.2328 * 24) Qm = 991.42 GPM
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Fundamentos Caudal de Slurry
% Solidos vs Dry solids 2000 tons per day Gravedad Especifica Sl Cw% Ss Sm
1.00 60 2.70 1.6071
Qm = 4.4 * 2000 / (0.6 * 1.6071 * 24) Qm = 380.26 GPM
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Fundamentos Presión y TDH de Slurry
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Reynold for Slurry Fluids
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Viscosidad Aparente
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Viscosidad Aparente
Volumen m3 Liquido Cubo 1m3 Esfera m3 Solido ߨ (4/3) r3 0.53 Cv 53% 47
Viscosidad Aparente (Video)
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Viscous tailing Slurry (100% fines < 75 um)
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Viscosidad
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Brookfield Viscosímetro – Low Shear
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Hércules Viscosímetro – High Shear
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Hércules Viscosímetro – High Shear
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Viscosímetros Rotacionales
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Viscosímetros Rotacionales
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Viscosímetros Rotacionales
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Curvas de Fluidez
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Viscosidad – Non Newtonian fluids
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Análisis Granulométrico Etapas del Proceso de Conminución Las etapas de la conminución son el Chancado y la Molienda. Existe un límite para el cual los chancadores son eficientes y, pasado éste, se utilizan los molinos, los que realizan la reducción de material para tamaños más finos. CHANCADO 1º 1% de Mandíbulas Mineral de Cobre Giratorio CHANCADO 1º Mandíbulas Impacto Giratorio
CHANCADO 2º Cono estándar CHANCADO 2º Impacto Cono Estándar Impacto
Impacto
R.O.M.
4040" inch Roca Mineralizada
CHANCADO 3º Cono cabeza CHANCADO 3º cortaCono Cabeza Corta De eje vertical Rodillos
MOLIENDA MOLIENDA
Rodillos
6" - 8"
1" 1 -–2"2
6 – 8 inch
inch
1/2" - 3/4"
1/2 – ¾ inch
150 - 300 um
150 – 300 μm
1” (pulgada)= 2,54 cm 1 μm (1 micrómetro)= 10-6 m BOMBAS DE LODOS
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Análisis Granulométrico
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Análisis Granulométrico Tamizado
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Análisis Granulométrico D50 (Video)
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Análisis Granulométrico Por Difracción de Laser ..\Procesos\Slurry\Calculation\20059623230131laser.pdf
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Análisis Granulométrico D50 (Grafica)
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Análisis Granulométrico Tamaño de Partícula
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Análisis Granulométrico Tamaño de Partícula
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Forma de Solidos
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Forma de Solidos
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D50 Microscopio Metalografico
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Tipo de flujo D50 vs Ss
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V
Cw
Cv
Régimen de flujo
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Tipo de flujo en tubería
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Tipo de flujo en tubería
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Tipo de flujo en tubería
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Tipo de flujo en tubería
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Tipo de regímenes de velocidad en Lodos.
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Tipos de regímenes de velocidad en Lodos.
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Tipo de flujo D50 vs Ss
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Impeller Tip Speed vs Severidad de Servicio
94m
65m
73m
55m
40m 70%
70%
30%
37m
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40m
34m
27m
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Desgaste de Partes
Desgaste ≈
Cv x (RPM)
2.50
BHN
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Calculo basicos en bombas de lodos
3.1
Calculo de NPSHr
3.2
Calculo de Velocidad de Sedimentacion
3.3
Calculo de TDH.
3.4
Correcion de Performance.
81
NPSHa : Slurry en base acuosa. NPSHa = ( Patm – Pvapor ) + Hestatica succ – hf GE Slurry GE Slurry : GE Mezcla Solido / Liquido. Patm : Presión atmosférica en mts de columna de agua. Pvapor : Presión vapor en mts de columna de agua. Hestatica succión: Altura en mts columna de Slurry. hf : perdidas primarias y secundarias en mts columna de Slurry.
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NPSHa : Slurry en base acuosa.
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Critical Carrying Velocity
The Mean Velocity of a Slurry in a Given Size Pipe, Above Which, the Solids Remain in Suspension, and Below Which the Solids Settle to the Bottom of the Pipe.
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Main correlations for Critical Carrying Velocity
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Velocidad de Sedimentación en tubería Wilson
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Velocidad de Sedimentación en tubería Wilson
D 6 inch D50 0.20mm Ss 3.4 Sm 1.2328 Cw 30 Cv 13.7 V
2.6 m/seg
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Durand’s and Cave’s limiting settling Velocity in Piping
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Durand’s limiting settling Velocity in Piping
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Durand’s limiting settling Velocity in Piping
D 6 inch D50 0.20mm Ss 3.4 Sm 1.2328 Cw 30 Cv 13.7 Fl 1.25 V
3.3 m/seg
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Cave’s limiting settling Velocity in Piping
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Cave’s limiting settling Velocity in Piping
D 6 inch D50 0.20mm Ss 3.4 Sm 1.2328 Cw 30 Cv 13.7 Fl 1.04 V
2.8 m/seg
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Cave’s limiting settling Velocity in Piping
D D50 Ss Sm Cw Cv Fl D50 V
6 inch 0.20mm 3.4 1.2328 30 13.7 1.05 rango 0 – 0.8mm 2.8 m/seg BOMBAS DE LODOS
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WASP’s limiting settling Velocity in Piping
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WASP’s limiting settling Velocity in Piping
D 6 inch D50 0.20mm Ss 3.4 Sm 1.2328 Cw 30 Cv 13.7 Fl’ 2.174 Fl 0.719 V
1.92 m/seg BOMBAS DE LODOS
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Oroskar and Turian Critical Velocity
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Wilson’s Deposition Velocity in Piping
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Material de la Bomba
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5500 XHD SRLXT SRLC
Tipo de Bomba SRL/ SRLC
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Dureza Escala Mohs
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Correlaciones mas Usadas Caída de Presión
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Perdida de Presion
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Slurry TDH Calculation
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Slurry TDH Calculation – Heterogenous flow
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Drag coefficient
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Drag coefficient
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Drag coefficient
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Drag coefficient
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Slurry Correction SETTLING SLURRY
NON-SETTLING SLURRY
Slurries with large size particles
Slurries with mostly fine particles
Non Homogeneous
Mostly Homogeneous
Require higher pipe velocities
Can be pumped at lower pipe velocities
Losses mainly due to particle rotation
Losses due to slurry slippage
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Caída de Performance en Bomba de Lodos Método HI de Corrección en Lodos Non – Settling homogeneo Newtoniano. Método de Corrección en Lodos Non – Settling homogeneo No-Newtoniano. Método HI de Corrección en Lodos Settling heterogeneo.
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Método HI de Corrección en Lodos Non – Settling homogéneo Newtoniano. (Método Fluido Viscoso)
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Método HI de Corrección en Lodos Non – Settling homogéneo Newtoniano. (Método Fluido Viscoso)
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Método de Corrección en Lodos Non – Settling homogeneo No-Newtoniano
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Caída de Performance Lodos Heterogéneos
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Método HI de Corrección en Lodos Settling Heterogeneos
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Método HI de Corrección en Lodos Settling Heterogéneos Rh1 = 1 - 1 / (0.6233 + 0.6027 * D50^0.1575) Rh2 = 122 * Diámetro impulsor ^ -0.663 30.7334
Rh
= Rh1 x Rh2
D50
mm
Diam impul
inch
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Método HI de Corrección en Lodos Settling Heterogeneos
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Método HI de Corrección en Lodos Settling Heterogéneos Hr = 1 - Rh x Ccv x Cs x Cfp
Hr = Nr Hr : Corrección en TDH. Nr : Corrección en Eficiencia. BOMBAS DE LODOS
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Método HI de Corrección en Lodos Settling Heterogéneos Cw GE Slurry D50 mm Diam inch Rh GE Solids Fine Part % Cv Rh
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20 1.176 4 8 4 5 5.882
0.27 1.00 0.27 1.47 0.90 0.39 0.85817
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Método Mc Elvain Cave de Corrección en Lodos Settling Heterogeneos
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Método Sillgren de Corrección en Lodos Settling Heterogeneos
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Conceptos basicos Altura sobre el nivel del mar.
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Numero de Reynolds
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TYPES OF SLURRY FLUIDS
NEWTONIAN
NON-NEWTONIAN
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Newtonian Fluids When the ratio of shear stress to shear rate is a constant for all shear rates, is independent of time, and zero shear rate exists only at zero shear stress.
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Non-newtonian fluids
Plastic Pseudo-plastic Dilatant Thixotropic Rheopectic
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Plastic When the shear stress to shear rate is constant for rates above zero and is independent of time, but when shear occurs only for shear above a fixed minimum value greater than zero.
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Pseudo-Plastic
When the ratio of shear stress to shear rate decreases as shear rate increases, is reversible and independent of time, and zero shear rate occurs only at zero shear stress.
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Dilatent
When the ratio of shear stress to shear rate increases as shear rate increases, reversibly and independent of time.
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Thixotropic
When the ratio of shear stress to shear rate decreases as time increases, dependent of time.
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Rheopectic
When the ratio of shear stress to shear rate is constant for all shear rates at any given instant of time, but increases with time.
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Comparacion Newtonianos – No Newtonianos
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Real World Slurries
In the real world, plastic slurries tend to be a combination of both the plastic and pseudoplastic slurry.
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Correlaciones de Fluidos No Newtonianos
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Non – Newtonian Examples
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Reologia diferentes lodos
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Reologia diferentes lodos
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Bingham plastic slurries
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Bingham plastic A Bingham plastic is a viscoplastic material that behaves as a rigid body at low stresses but flows as a viscous fluid at high stress. It is named after Eugene Bingham who proposed its mathematical form. It is used as a common mathematical model of mud, slurries flow in offshore engineering, and in the handling of slurries. A common example is toothpaste, which will not be extruded until a certain pressure is applied to the tube. It then is pushed out as a solid plug.
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Velocidad Critica en Lodos No-Newtoniamos Tipo Bingham
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Reograma
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Velocidad de Sedimentación Fluidos No Newtonianos
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TDH Correlaciones en Slurries tipo Bingham
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Bingham Correlaciones Flujo Laminar
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Bingham Correlaciones Flujo Turbulento
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Bingham Correlaciones Flujo Laminar
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Bingham Correlaciones
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Teoria de funcionamiento 4.1
Tipos de Servicio.
4.2
Principio de funcionamiento.
4.3
Criterios de Diseño de Bombas.
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HORIZONTAL SLURRY PUMPS Vary by Design Type, Wear Material and Service H.I. Service Classes – Class I – Mine Dewatering – Thickener Overflow
– Class 2 – Filter Feed – Slurry Transfer – Flotation
– Class 3 – Thickener Underflow – Tailings
– Class 4 – Primary Grinding – SAG Mill – Secondary Grinding – Ball Mill
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HORIZONTAL SLURRY PUMPS SERVICES 80%
Extra Heavy Severe Duty Class4
71% 66% 54%
Heavy Duty Class 3 Medium Duty Class 2 Light Duty Class 1
46% 38%
43%
27% 15%
11%
75
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HORIZONTAL SLURRY PUMPS SERVICES 80%
Extra Heavy Severe Duty Class4
71% 66% 54%
Heavy Duty Class 3
46%
Medium Duty Class 2
27%
Light Duty Class 1
72%
38%
15%
34%
8%
100
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HORIZONTAL SLURRY PUMPS SERVICES 80%
Extra Heavy Severe Duty Class4
71% 66% 54%
Heavy Duty Class 3
46%
Medium Duty Class 2
27%
54%
38%
23%
15%
Light Duty Class 1
7%
200
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HORIZONTAL SLURRY PUMPS SERVICES 80%
Extra Heavy Severe Duty Class4
71% 66% 54%
Heavy Duty Class 3
46%
Medium Duty Class 2
27%
39%
38%
15%
15%
4%
Light Duty Class 1
300
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Teoria de Bombas Centrífugas de Lodos Principio de Funcionamiento CASING-CARCAZA FORROS
(1)
IMPELLER-IMPULSOR CERRADO
(2)
EJE (1)
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Teoria de Bombas Centrífugas Principio de Funcionamiento Para cuestiones practicas:
TDHbomba ≈ V
2
2g
V : IMP. TIP SPEED RPM 1800 D 10.22 inch
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Teoria de Bombas Centrífugas Principio de Funcionamiento
Altura Diametro
RPM 2
Altura (pies) =
Diam (Pulg) x RPM 1838
Esto es solo aproximado y aplica de manera mas certera a Bombas de bajo numero Especifico de velocidad
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Teoria de Bombas Centrífugas Impeller Tip Speed D 29” 98.1 FPS 150 FT 775 rpm D 21” 98.1FPS 150FT 1070 rpm D18” 98.2FPS 150FT 1500 rpm BOMBAS DE LODOS
Teoria de Bombas Centrífugas Impeller Tip Speed
29”
• • • • •
21”
15”
D 29” 86.1 FPS 115 FT 680rpm 5166 FPM D 21” 86.8FPS 117 FT 947rpm 5210 FPM
6 inch diameter discharge pumps. 1000 GPM @ 125 FT. Pumps speed varies from 650 rpm to 1400 rpm. D15” Tips varies from 86 fps to 90 fps. 90.5FPS 127 FT Hystories shows that pump with 29 inch 1383rpm 5435FPM Diameter impeller will outlast pump with 15 inch 6 : 1
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5500 15 inch 90.5 FPS 125 FT 1383 rpm Ns 1400 81%BEP
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5500 21 inch 86.8FPS 125 FT 947 rpm Ns 990 77%BEP
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5500 29 inch 86.1 FPS 125 FT 680 rpm Ns 606 95%BEP
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Dimensionamiento Bomba de Lodos mm
lbs
mm
rpm
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rpm
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Impeller Tip Speed vs Severidad de Servicio
94m
65m
73m
55m
40m 70%
70%
30%
37m
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50m
40m
34m
27m
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Selection Guidelines Rubber Lined Pumps
* Higher peripheral velocities possible with hard metal or polyurethane Impellers
BOMBAS DE LODOS
Desgaste de Partes
Desgaste ≈
Cv x (RPM)
2.50
BHN
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Desgaste de Partes
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Slurry Pump Design
BOMBAS DE LODOS
Slurry Pump Design Slurry Cutwaters are Less Pronounced. Larger Flow Passages. CFD design to reduce high velocity zones, and recirculation zones. Closed impellers are preferred. To reduce suction impeller recirculation, impeller radial clearence adjustment is used instead Wear rings. Wear parts are used. Pedestal design for bearing frame support. BOMBA DE LODOS
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Slurry Pump vs Process Pump
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Slurry Pump vs Process Pump BackPlate
BOMBA DE LODOS
Casing
Slurry Pump vs Process Pump BackPlate
Casing
Suction Liner
Suction Cover
BOMBA DE LODOS
Slurry Pump vs Process Pump
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Slurry Pump vs Process Pump
BOMBA DE LODOS
Slurry Pump vs Process Pump
SLURRY
PROCESS
BOMBA DE LODOS
Slurry Pump vs Process Pump
PROCESS
BOMBA DE LODOS
SLURRY
Slurry Pump Design Material
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Slurry Pump Design Material – Rubber Lined Slurry Pump
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Slurry Pump Design Material – Rubber Lined Slurry Pump
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Slurry Pump Design Material – Rubber Lined Slurry Pump
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Slurry Pump Design Material – Metal Unlined Slurry Pump
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Slurry Pump Design Material – Metal Unlined Slurry Pump
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Slurry Pump Design Casing Los fabricantes de equipos han logrado diseños, para atenuar el desgaste y hacer más eficiente sus equipos según la aplicación y clase de servicio donde se utilice. El HI reconoce el siguiente cuadro, y recomienda seleccionar los equipos siguiendo estos parámetros.
Anular
Semivoluta
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Voluta Convencional
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Slurry Pump Design Casing
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Slurry Pump Design Casing
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Slurry Pump Design Casing – Front Pull Out – Radial Split
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Slurry Pump Design Casing – Front Pull Out – Radial Split
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Slurry Pump Design Casing – Front Pull Out – Radial Split
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Slurry Pump Design Casing – Front Pull Out – Radial Split
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Slurry Pump Design Impeller Design
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Slurry Pump Design Impeller Design
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Slurry Pump Design Impeller Design
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Slurry Pump Design Impeller Design
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Slurry Pump Design Impeller Design
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Slurry Pump Design Wear Parts Back Casing Liquid End
Partes de Desgaste Liquid End Front Casing Liquid End
Pedestal Power End Closed Impeller Liquid End
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Slurry Pump Design Extra Thickness Wear Parts
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Slurry Pump Design Hydraulic Coverage
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Slurry Pump Design Hydraulic Coverage
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Slurry Pump Design CFD Tool Design
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Tipos de Bombas de Lodos
5.1
Tipos Principales.
5.2
Componentes Principales
5.3
Portafolio Bombas Goulds
3.4
Correcion de Performance.
202
Tipos de Bombas de Lodos
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Tipos de Bombas de Lodos
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Tipos de Bombas Centrifugas
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Componentes Principales
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Bomba de Lodos Horizontal Componentes Principales
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Shaft Seals
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Vertical Cantilever Sump Pumps
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OH0 Overhung flexibly coupled single stage lined
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XHD SRL
5500 3196
Bombas Centrifugas Bomba de Lodos
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VRS VJC
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Sectional View Lined Pump
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Metal lined Pump Closed Impeller
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Rubber Lined Pump Open Impeller
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Rubber Lined Pump Closed Impeller
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Rubber Lined Pump Closed Impeller
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Rubber Lined Pump Extra Thickness Liners Closed Impeller
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Sectional View Unlined Pump
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Metal Unlined Pump Closed Pump
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Open Rubber Impeller Slurry Pump
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Close Rubber Impeller Slurry Pump
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Close metal impeller Vista Expandida.
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Arreglo de Bomba - Motor
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Goulds Pumps Slurry Pumps – Portfolio. Horizontal Rubber Lined Pump SRL Series SRL, SRL-M, SRL-C, SRL-CM, SRL-XT, Horizontal Froth Rubber Lined Pump SRL-S. Vertical Cantilever Rubber Lined Pump VRS. Horizontal Metal Lined Pump Extra Heavy Duty XHD.
SRL-C
5500
XHD
VRS
Horizontal Metal Unlined Pump Heavy Duty Closed Impeller 5500. Medium Duty Open Impeller JC. Vertical Cantilever Metal Unlined Pump VJC.
BOMBAS DE LODOS
Model SRL Family Product Description High Efficiency Slurry Pumps Low power costs, proven hydraulics & reliable operation Thick Bolt-In Rubber Liners Field replaceable, positive assembly and long wear life Large Diameter Impellers Lower operating speeds & extended wear life
SRL-C
SRL
Heavy Duty Bearing Assembly Low shaft deflection, adjustable for peak operating efficiency Packed Gland / Mechanical Seal Choice of packing arrangements or mechanical seals BOMBAS DE LODOS
SRL-S
SRL-XT
SRL / SRL-M / SRL-C / SRL-CM / SRL-XT / SRL-S Size & Type Designation Example - 14x12-29 SRL-CMHD
– 14 – 12 – 29 – SRL –C –M – HD – XHD
= Suction Size in Inches = Discharge Size in Inches = Impeller Diameter in Inches = Soft Rubber Lined = EnClosed Impeller = Metal Impeller = High Pressure Duty Casing = EXtra High Pressure Duty Casing
* The Pump Size & Type is Cast in Raised Letters on the Suction Casing * The Old Design does not have the Impeller Diameter included on the Casting BOMBAS DE LODOS
Model SRL Hydraulic Coverage Flow to 1,500 gpm (341 m3/hr) Head to 135 feet (41 m) Pressure to 232 psig (1600 kPa) 4 Sizes.
BOMBAS DE LODOS
Model SRL-C Key Features and Benefits High-Efficiency Design Very low power costs Proven hydraulics for slurry service Extended parts wear life Thick bolt-in liners Positive assembly in casing for extended life Large liners reinforced with a fiberglass shell Resist liner collapse under adverse conditions Parts Interchangeability Many parts are interchangeable between pump sizes built on the same bearing frames.
Replaceable suction wearplate available on 6” (150mm) and larger pumps Provides reduced downtime and lower replacement cost
Large diameter closed impeller Lower speeds and extended wear life Axially adjustable bearing assembly Maintains peak operating efficiency and life Short, rigid shaft and heavy duty bearings Low-deflections and reliable service Packed gland option or mechanical seal Standard, low, or no Dilution arrangements Precision-machined cast iron frame Standard, low, or no Dilution arrangements Five discharge positions available Suitable for most piping arrangements
Model SRL-C Hydraulic Coverage Flow to 20,000 gpm (4,542 m3/hr) Head to 164 feet (50 m) Pressure to 400 psig (2,758 kPa) 8 Sizes. Heavy Duty Design.
BOMBAS DE LODOS
SRL-C Wet End Features Hybrid Liners Standard on 12x10-25 and larger SRL-C Pumps - Provides Steel Plate as Base for Liner Including Cutwater. - Composite Liner for Volute Area to Resist Collapse due to System Upset and Ease of Handling. - Space Between Steel Plate and Composite Allows some Flexing for Installation and Fit. - Finished Gland Side Liner
BOMBAS DE LODOS
230
Model SRL – SRL-C
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Model SRL-XT EXtra Thickness Rubber Lined Pump Extra rubber thickness for severe service. Removable suction cover easy maintenance. Liners positively locked into casing for better liner fit. Impeller release collar for less removal impeller time. SAG and Ball mil service longer cycle life.
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Model SRL-XT Hydraulic Coverage EXtra Thickness Rubber Lined Pump Flow to 10,000 gpm (2,270 m3/hr) Head to 140 feet (42 m) Pressure to 250 psig (1725 kPa) 4 Sizes. Solids to: ½” ,13 mm. Sizes to 6” to 12”. Extra heavy duty design. BOMBAS DE LODOS
Model SRL-XT Mill Circuit Pump
Primary Grinding
Secondary Grinding
SAG Mill
Ball Mill
Output: Very Coarse Ore
Output: Coarse Ore
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SRL-XT Pumps Impeller Release Collar
Releases the Torque Load on Impeller Threads to
Tapped holes for jacking
Facilitate Disassembly Tapered at the Shaft Sleeve for Easy Removal Allen Head Screws for Collar Assembly & Removal Also Functions as Deflector
BOMBAS DE LODOS
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SRL / SRL-C / SRL-XT
Wet End Features Front Pull-out Design CW Rotation No Vent, Drains, or Taps in Casing Packed Box Standard Hard Coated 316 SS Shaft Sleeve Standard
BOMBAS DE LODOS
236
SRL / SRL-C / SRL-XT – Shaft Sleeve XH-800 Shaft Sleeve Standard on all SRL pumps Hard Ni-Cr coating – 64 Rc Will not chip or crack Base 316 SS alloy for corrosion resistance Ground 6-8 RMS finish Other alloys available BOMBAS DE LODOS
237
SRL / SRL-C / SRL-XT
Wet End Features Front & Rear Casing Halves Cast Iron Casing is Standard Ductile Iron & Carbon Steel Casings Available for Higher Pressures up to 400 PSI Standard 75 - 140 PSI HD, DI 225 - 250PSI XHD, Steel 250 - 400PSI
BOMBAS DE LODOS
No se puede mostrar la imagen en este momento.
238
SRL / SRL-C / SRL-XT Wet End Features Bolt-In Liners Suction Wear Plates and Suction Liners on 8x6 and larger sizes 2 Piece Gland Side Liner on 16” & 20” Pumps
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SRL / SRL-C / SRL-XT
Impeller Features -Threaded on Impellers -Semi-open Impellers on SRL -Closed Impellers on SRL-C
Shearpeller
-Shearpellers Available on select sizes -Chrome Iron and Alloys Available on most sizes
BOMBAS DE LODOS
240
SRL-C / SRL-XT Ceramic Rubber Media Pump suction wear plate in natural rubber with ceramic rods molded in. – Offers hard surface with the resilience of natural rubber
– 2-4 times life, less downtime – Maximizes pump performance
BOMBAS DE LODOS
SRL-S – ShearpellerTM Froth Rubber Lined Pump
BOMBAS DE LODOS
SRL-S – ShearpellerTM Froth Rubber Lined Pump Unique impeller design to handle slurries with froth / entrained air or long / stringy particles – Replaces standard impeller – Larger pump not required – Variety of materials available
BOMBAS DE LODOS
SRL-S – ShearpellerTM Froth Rubber Lined Pump - Hydraulic Coverage Flow to 16,000 gpm (3,630 m3/hr) Head to 125 feet (38 m) 8 Sizes.
BOMBAS DE LODOS
SRL-S – ShearpellerTM Unique in design Pd
Ps
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SRL-S – ShearpellerTM Froth Factor Common in Mineral Processing Operations Where Froth Flotation is used. Froth Contains a Large Amount of Air and can Cause Pumping Problems. The Full Volumetric Flow Divided by the Liquid Content is Know as the Froth Factor (think bucket of suds). Typical Froth Factors are in the 1.2 – 3 Range but Factors as High as 5 may Occur. A Standard Centrifugal Pump Must be Oversized to Deal with this.
BOMBAS DE LODOS
SRL-S – ShearpellerTM Froth Factor – Pump Sizing Multiply Flow Rate Times Froth Factor to Get Required Pump Flow. TDH Remains the Same. Horsepower is Calculated Using the Actual Capacity and Efficiency. Motor Should Be Selected as Non-Overloading (One of the few Cases Where this is Required When Pumping a Slurry). One Alternative to this is the Shearpeller™ Which will be Discussed with the SRL Pump Line later.
BOMBAS DE LODOS
SRL-S ShearpellerTM Ps 14.7psia Pd 55.6psia Vd/Vs= 3.8
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SRL Series Liners Various Elastomers Available - Natural - Nitrile - Neoprene - Chlorobutyl - Hypalon - Urethane Elastomers Molded to Metal Skeletons
BOMBAS DE LODOS
Metal Skeletons
SRL Series Casing Configuration Wet End Features 5 Discharge Positions Available (A -E) • A - Top Horizontal • C - Vertical Up - Std. • E - Bottom Horizontal • B & D - 45º Discharge
BOMBAS DE LODOS
250
SRL Series Power Frames 8 Sizes of Power
Frame 0 Frame 1
Frames
Frame 2 Frame 3 Frame 4
Rubber Parts & Casings are not interchangeable between pump types
Frame 5 Frame 6 Frame 7
2x2-10 3x3-10 SRL 3x3-10 SRL-C 5x4-14 SRL-C 5x5-14 SRL 6x6-15 SRL 8x6-18 SRL-C 10x8-21 SRL-C 6x6-21 SRL-XT 12x10-25 SRL-C 8x8-25 SRL-XT 14x12-29 SRL-C 10x10-28 SRL-XT 16x14-34 SRL-C 20x18-40 SRL-C 14x12-36 SRL-XT*
* Frame 7 shaft & bearing assembly on frame 6 pedestal BOMBAS DE LODOS
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SRL Series Power Frame - Features Power Ends Cartridge Bearing Frame Bearing Housing Integral with Pedestal on 2x2-10 External Impeller Adjustment Large Diameter Shaft Motor Base Mounts off Pedestal Oil Level Sight Glass on both sides
BOMBAS DE LODOS
252
SRL Series – Hydraulic Coverage
BOMBAS DE LODOS
SRL Series Optional Features
BOMBAS DE LODOS
SRL/SRL-XT Typical Applications/Installations
BOMBAS DE LODOS
Model SRL Typical Applications Mining Mineral Processing Pulp & Paper Aggregate Power Utility Chemical Applications General Industry
BOMBAS DE LODOS
Predicted Curve – 24x22-44 SRL-C
BOMBAS DE LODOS
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Predicted Curve – 28x26-50 SRL-C
BOMBAS DE LODOS
258
Model 5500 Product Description Extra Heavy Duty Unlined Metal Horizontal Slurry Pump Large Diameter Impeller develops higher heads at lower operating speeds. Extra Thick Wet End Components for extended wear life. Improvement Inlet Impeller Design for lower wear. Extra Heavy Duty Casing for maximum wear life. Extra Heavy Duty Shaft assures minimum shaft deflection. Sealing Flexibility Choice of packing, mechanical seal or dynamic seal. Wear Tests Aluminum models utilized. L-10
Min. 100,000 hours bearings. BOMBAS DE LODOS
Model 5500 Hydraulic Coverage Extra Heavy Duty Unlined Metal Horizontal Slurry Pump Flow to 17,000 gpm (3,861 m3/hr) Head to 425 feet tdh (139 m) Temperature to 250° F (121° C) Pressure to 500 psig (3,448 kPa) Solids to 5 inches (127 mm) Materials: HC600, 1269,1650, CD4MCu 24 sizes Spherical Solids Up to 4 Inch Available 4 power frames
BOMBAS DE LODOS
Model 5500 Key Features and Benefits Extra Heavy Duty Shaft Long bearing span and large diameters reduce shaft deflection, extend bearing and packing life. Ideally suited for mounting large motors overhead. Shaft Sleeve Hook-type, extra thick and hardened for long life and reduced maintenance. Optional ceramic sleeve available for severe services. Full T-Slot Bolting For ease of maintenance.
Knock-Off Deflector For easier impeller removal and added bearing protection.
Integral Rear Liner No joints; extra thick. Reduces parts inventory cost and simplifies maintenance.
Cast In Lifting Lugs Provide safe, ease of handling Stuffing Box Connections Standard for either “full flush” or “low dilution.” Customer selects best choice for service. Positive Impeller Attachment Heavy duty Acme threads for easy impeller removal. No inserts for trouble-free operation.
Thick Metal Sections Casing, suction cover and impeller have extra thick wall sections for extended wear life, reduced maintenance.
Large Diameter Impeller Higher heads at lower operating speeds. Extra thick wall sections.
Model 5500 - Casing T-Slot Bolting Easy Removal & Assembly. Thick Sections Long Wear Life. Integral Rear Wall No Joint - Reduced Wear. Lifting Lugs Ease of Maintenance.
BOMBAS DE LODOS
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Model 5500 - Impeller Large Diameter Lower Speed & Less Wear Large Adjustment Maximizes Life Large Eye Area Longer Wear Life Acme Threads Easy Impeller Assembly Curved Inlet Smooth Flow Transition No BPOVs Higher Efficiency
BOMBAS DE LODOS
263
Model 5500 – Suction Cover Machined Taper Ease of Removal Contoured Less Recirculation & Higher Efficiency Can be Rotated Maximize Wear Life Ceramic Inserts Available on Certain Sizes Cast-in Lifting Lugs Safety & Maintenance
BOMBAS DE LODOS
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Model 5500 - Stuffing Box Large & Open Easy access. Release Collar Easier impeller removal. Packing Options Full flush or weep. Dry Gland Option Expellers available. Slurry Seal Taper design box available. Shaft Sleeve Hardened 420SS hook type.
BOMBAS DE LODOS
265
Model 5500 – Bearing Frame Dead-Set Bearings No shims or preload needed. Oil Lube Standard. Register Fit Positive alignment to frame. Large Shaft Ø Minimal deflection. Bearings Double row tapered, & spherical rollers. Shaft Sealing Two lip seals w/ grease. Pump Base Free-standing fabricated. 266
5500 – Front Pull Out Extra Heavy Duty Unlined Metal Horizontal Slurry Pump
BOMBAS DE LODOS
Model 5500 HP – High Pressure Extra Heavy Duty Unlined Metal Horizontal Slurry Pump
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5500 - Long Life Design Extra Heavy Duty Unlined Metal Horizontal Slurry Pump Feature
Function
Benefit
Heavy Duty Design
Designed for the most severe slurry applications
Reduced Downtime Maximum Reliability Reduced Costs
Free Standing Pump
Not bedplate or special support required
Easy Installation Reduced Installation Costs
Large Heavy Duty Power End Overhead Motor Mounting
Designed for maximum life and load. Allows motor to be mounted directly above frame, minimizing space requirement. Can overhead mount largest motor frames in industry.
Increased reliability Reduced installation costs.
Cartridge Bearing Frame
Allows for quick power end change out, Allows for axial adjustment of impeller
Reduced maintenance, Less downtime
Dead Set Bearings
Eliminates shims, adjusting rings, and springs
Easier, simplified maintenance, less downtime
No Liners
Fewer Joints Fewer Parts to Stock Easier Maintenance, no fit problems it outer shell wears
Lower overall costs Less Downtime Easier Maintenance
Knock Off Deflector
Protects bearings Facilitates impeller removal
Increased reliability Reduced Downtime Ease of Maintenance
Open Stuffing Box Area
Easy access to packing or mechanical seal
Ease of maintenance
Designed to be Maintenance Friendly
Incorporate features that makes the 5500 the easiest and safest pump to maintenance on the market
Ease of Maintenance Less downtime Reduced costs Increased Safety
BOMBAS DE LODOS
Model 5500 Typical Applications -Primary Metals -Coal Preparation -Non-Metallic Mining -Sand and Gravel -Power Utility -Wet Process Cement -Pulp & Paper -General
BOMBAS DE LODOS
Model 5500 Typical Applications
BOMBAS DE LODOS
Model 5500 HP – Application Extra Heavy Duty Unlined Metal Horizontal Slurry Pump
BOMBAS DE LODOS
272
Model JC Product Description Thick Wet End Components For extended wear life. Replaceable Wear Liner Low maintenance cost. Heavy Duty Power End Increased mean time between failures. External Impeller Adjustment Maintains original efficiency; simple and fast. Maximum Parts Interchangeability Entire line uses just five power ends. Sealing Flexibility Choice of packing, mechanical seals or dynamic seal. Standard Construction HC600, High Chrome Iron.
BOMBAS DE LODOS
Model JC Hydraulic Coverage Flow to 7,000 gpm (1,600 m3/hr) Head to 240 feet tdh (73 m) Temperature to 250° F (120° C) Pressure to 150 psig (1,034 kPa) Solids to 2.25 inches (57 mm) Materials: Cast Iron, HC600, 1269, 316SS, CD4MCu 15 sizes. Medium Duty. BOMBAS DE LODOS
Model JC Key Features and Benefits Suction Cover Liner Replaceable part takes all wear on suction side of casing
Casing Extra thick wall sections for extended wear life, reduced maintenance. Dual volute design where necessary to reduce radial loads.
External Impeller Adjustment Maintains maximum efficiency by simple adjustment.
Impeller Best design for slurry services/proven by wear testing and field experience. Back pump-out vanes reduce stuffing box pressure, keep solids out of stuffing box. Discharge Nozzle May be rotated in field to any of eight positions.
Shaft Sleeve Hook-type design for shaft protection.
Bearings Radial and thrust bearings are sized for 3-year B10 life (25,000 hours). Grease or oil lubrication.
Heavy Duty Shaft Large diameters to handle high loads, reduce shaft deflection
Dynamic Seal Expeller option for absolute dry box sealing. No outside flush required.
Mechanical Seal A wide range of mechanical seals is available for sealing flexibility..
JC Features
BOMBAS DE LODOS
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JC Typical Services Light to medium duty slurries
– Corrosive – SG 1.3 – SG 1.4 below 1200 rpm
– Entrained air to ~ 6%
BOMBAS DE LODOS
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Model JC S Box - Bearing Frame Heavy Duty Bearing Frame One piece for extended wear life. External Impeller Adjustment Maintains original efficiency; simple and fast Replaceable Wear Liner Low maintenance cost. Sealing Flexibility Choice of packing, mechanical seals or dynamic seal. Rugged Shaft Heavy duty design.
BOMBAS DE LODOS
JC Mounting Options
BOMBAS DE LODOS
279
Model JC Typical Applications Wet Scrubber Systems Waste Sludge Fracing Slurries (Oil Field) Paper Mill Wastes and Liquors Clay and Sand Slurries Dirty Water Kaolin Clay Carbon Slurry Lime Mud Precipitated & Ground CaCO3
BOMBAS DE LODOS
XHD Extra Heavy Duty Slurry Pump Horizontal Lined Metal Pump Full Metal Lined For extended wear life. Replaceable Wear Metal Liners Low maintenance cost. Heavy Duty and Compact Power End Increased mean time between failures a easy for replacement. External Adjustable ring Without stop the pumps and maintains original efficiency; simple and fast. Standard Construction HC600, High Chrome Iron. I-Frame For Vibration & Temperature condition monitoring.
BOMBAS DE LODOS
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XHD Extra Heavy Duty Slurry Pump Horizontal Lined Metal Pump Six Sizes
4x3, 6x5, 8x6, 10x8, 12x10 & 14x12.
Wide Capability
Flows to 4000 m3/h, Heads to 100m, 17 bar.
Low Specific Speeds 1200-1425.
Currently 3 power frames PF2, PF3, PF4.
BOMBAS DE LODOS
XHD Extra Heavy Duty Slurry Pump Horizontal Lined Metal Pump
283
XHD - Low Water & Energy Consumption Horizontal Lined Metal Pump Impeller adjustment to set suction clearance and reduce recirculation
Efficient Hydraulic Design
One piece HC600 suction wear plate for longer life
Low water seal options (1L4 water flush, slurry mechanical, and dynamic
BOMBAS DE LODOS
XHD - Maximizing Productivity Horizontal Lined Metal Pump Quick change wet end cartridge to reduce downtime.
Pump out vane designs to reduce solids abrasion of the nose gap.
One piece stuffing box
On-board condition monitoring (Optional)
BOMBAS DE LODOS
XHD - Maintenance Features Horizontal Lined Metal Pump Wide open seal area with split, removable gland.
HC600 alloy for suction wear plate to extend life
Easy access impeller adjustment Removable wet end cartridge.
Optional InproTM Seal bearing isolators
BOMBAS DE LODOS
Feedback From Early Field Placements Pumping Application
Slurry Type
What the Customer Said
Primary cyclone feed
Primary metals
“Like clockwork… absolutely great.”
Coal
“Uses 7 to 9 motor amps less… the flow coming out of the bin is greater out of the XHD than the pump we’re replacing.”
Aggregates
“Motor amps dropped to 175 amps with the product in the [XHD] system… normally they are running at 185 amps with this load.”
Coal
“Pumps work great. No problems and the XHD is easy to work on… the oil stays clean and the pumps run very quietly.”
Thickener underflow
Primary sand pump
Cyclone feed
BOMBAS DE LODOS
287
XHD – Impeller Adjustment Horizontal Lined Metal Pump (Video)
BOMBAS DE LODOS
5/2/2015
288
XHD – Wet End Removal Horizontal Lined Metal Pump (Video)
BOMBAS DE LODOS
5/2/2015
289
Goulds Pumps - Slurry Pumps Coverage XHD, 5500, SRL, SRL-XT, JC Slurry Pumps
BOMBAS DE LODOS
Why Use A Vertical Cantilever Pump? Eliminates Packing & Mechanical Seals Requires No Submerged Bearings Requires No In-Sump Lubrication Requires No Check or Foot Valves Is Easily Primed Can Run Dry Requires Minimal Maintenance Bearings & Motor Located Above Liquid Level Don’t Like Submersible Pumps
BOMBAS DE LODOS
Model VJC Vertical Cantilever Unlined Pump
Sizes: 2” - 10” Flows - to 8000 GPM Heads - to 240 Feet Solid Sizes: .875” - 2.25” 6 Sizes. Metal JC wet end Available in lengths up to 8-ft Four power frames.
BOMBAS DE LODOS
292
Model VJC Vertical Cantilever Unlined Pump Replaceable Suction Liner Enclosed Impeller on the 8” and 10” pumps Materials: CI, HC600, 316SS, Other - Consult Factory Double Volute Casing Except 2” Semi-Open Impeller on 2,3,4, & 6” pumps Impeller Threaded to Shaft Against Rotation Hub Throttle Bushing
BOMBAS DE LODOS
5/2/2015
293
Model VRS Vertical Cantilever Rubber Lined Sump Pump Rubber Lined Pump. Open impeller. Uses SRL wet end. Available in 4-ft & 6-ft lengths.
Five sizes (1½”, 2”, 3”, 5” & 6”).
Flows to 1500 usgpm (341 m3/hr).
Total heads to 120-ft (37m)
BOMBAS DE LODOS
5/2/2015
294
Model VRS Vertical Cantilever Rubber Lined Sump Pump Standard SRL Casings Standard SRL Liners Standard 4-ft and 6-ft Lengths Sizes to Cover Majority of Applications Higher Efficiency than Competition Very Price Competitive Floor Plate is Included Motor Mount & Guard Included Discharge & Suction Tail Pipes are Optional Adders BOMBAS DE LODOS
295
Model VRS Vertical Cantilever Rubber Lined Sump Pump
BOMBAS DE LODOS
5/2/2015
296
Vertical Cantilever Slurry Sump Pump Coverage.
BOMBAS DE LODOS
5/2/2015
297
Desgaste en Bomba de Lodos 6.1
Factores de desgaste.
6.2
Modos de desgaste.
6.3
Criterios de abrasividad.
6.4
Estimación del desgaste.
6.5
Desgaste a % BEP y Fotos. BOMBA DE LODOS
5/2/2015
298
SLURRY PUMP DESIGN KEY CONSIDERATIONS ROTATIONAL SPEED. RUBBER vs. METAL. CASING DESIGN. MODOS DE DESGASTE. SEVERIDAD DEL SERVICIO. FACTORES DE DESGASTE. % BEP POINT. MATERIALS OF CONSTRUCTION. PH, % CONCENTRATION, PH OF SLURRY. BOMBAS DE LODOS
SLURRY PUMP DESIGN ROTATIONAL SPEED Rotational Speed is the Single Biggest Factor in the Life of Slurry Pump Parts. That is Why Slurry Pumps are Not Applied @ 3600 rpm. All Other Things Being Equal, Wear Life Varies by the Speed Ratio to the 2.5 or 3 Power (ITT uses 2.5).
BOMBAS DE LODOS
SLURRY PUMP DESIGN PARTS LIFE EXAMPLE EFFECT OF ROTATIONAL SPEED CHROME IRON CASING --- 3.00” THICK CURRENT WEAR RATE
--- 0.0008” / HR
ROTATIONAL SPEED
--- 1480 RPM
ESTIMATED LIFE =
3.00/0.0008” = 3,750 HOURS
CONDITIONS CHANGE TO REDUCE PUMP SPEED TO 1000 RPM. SPEED CHANGE EFFECT = .0008 * (1000/1480)2.5 = .0003” NEW EST. LIFE = 3.0 / 0.0003” = 10,000 HOURS (2.7 x )
BOMBAS DE LODOS
SLURRY PUMP DESIGN IMPELLER TIP SPEED
BOMBAS DE LODOS
SLURRY PUMP DESIGN DESGASTE DE PARTES
Desgaste ≈
Cv x (RPM)
2.50
BHN
BOMBAS DE LODOS
5/2/2015
303
SLURRY PUMP DESIGN MODOS DE DESGASTE EN BOMBAS
BOMBAS DE LODOS
5/2/2015
304
SLURRY PUMP DESIGN MECANISMOS DE EROSION POR IMPACTO
BOMBAS DE LODOS
5/2/2015
305
SLURRY PUMP DESIGN EROSION POR IMPACTO
BOMBAS DE LODOS
5/2/2015
306
SLURRY PUMP DESIGN SLIDING EROSION
BOMBAS DE LODOS
5/2/2015
307
SLURRY PUMP DESIGN LUGARES DE TÍPICOS DE DESGASTE
BOMBAS DE LODOS
5/2/2015
308
SLURRY PUMP DESIGN LUGARES DE TÍPICOS DE DESGASTE
BOMBAS DE LODOS
5/2/2015
309
SLURRY PUMP DESIGN LUGARES DE TÍPICOS DE DESGASTE
BOMBAS DE LODOS
5/2/2015
310
SLURRY PUMP DESIGN LUGARES DE TÍPICOS DE DESGASTE
BOMBAS DE LODOS
5/2/2015
311
SLURRY PUMP DESIGN LUGARES DE TÍPICOS DE DESGASTE
BOMBAS DE LODOS
5/2/2015
312
SLURRY PUMP DESIGN SEVERIDAD DEL SERVICIO
BOMBAS DE LODOS
5/2/2015
313
SLURRY PUMP DESIGN SLURRY SPECIFIC GRAVITY FOR MILLER NUMBER EFFECT
BOMBAS DE LODOS
5/2/2015
314
Millers Number Some Slurries
BOMBAS DE LODOS
5/2/2015
315
SLURRY PUMP DESIGN MILLERS NUMBER SOME SLURRIES
BOMBAS DE LODOS
5/2/2015
316
SLURRY PUMP DESIGN MILLERS NUMBER
BOMBAS DE LODOS
5/2/2015
317
SLURRY PUMP DESIGN MILLERS NUMBER
BOMBAS DE LODOS
5/2/2015
318
SLURRY PUMP DESIGN MILLERS NUMBER
BOMBAS DE LODOS
5/2/2015
319
HORIZONTAL SLURRY PUMPS Vary by Design Type, Wear Material and Service H.I. Service Classes – Class I – Mine Dewatering – Thickener Overflow
– Class 2 – Filter Feed – Slurry Transfer
– Class 3 – Thickener Underflow – Tailings
– Class 4 – Primary Grinding – SAG Mill – Secondary Grinding – Ball Mill
BOMBAS DE LODOS
May 2, 2015
320
Hard Rock Mining- Slurry Service Class Ref: Copper
BOMBAS DE LODOS
WEAR TEST RESULTS RELATIVE LIFE FACTORS MATERIAL
AVG. BHN
RELATIVE LIFE
CAST IRON
170
1.0
316SS
155
1.1
CD4MCu
260
1.2
ALLOY 20
125
1.2
NI-HARD
652
2.3
HC600
675
3.1
CERAMIC
---
5.4
BOMBAS DE LODOS
RELATIVE LIFE FACTORS WEAR TEST RESULTS
BOMBAS DE LODOS
SLURRY PUMP LIFE FACTORS APPLICATION POINT APPLICATION POINT, METAL PUMP (% OF BEST EFF.)
LIFE FACTOR
0 TO 25
0.3
26 TO 50
0.5
51 TO 75
0.8
76 TO 100
1.0
101 TO 120
0.7
BOMBAS DE LODOS
HARDNESS OF COMMON MINERALS
BOMBAS DE LODOS
5/2/2015
325
WEAR LINED PUMP SECTIONAL VIEW
BOMBAS DE LODOS
5/2/2015
326
WEAR UNLINED PUMP SECTIONAL VIEW
BOMBAS DE LODOS
5/2/2015
327
WEAR IMPELLER
BOMBAS DE LODOS
5/2/2015
328
Suction Liner Wear
BOMBAS DE LODOS
5/2/2015
329
Impeller liner Wear
BOMBAS DE LODOS
5/2/2015
330
Casing Liner Wear
BOMBAS DE LODOS
5/2/2015
331
Casing Wear % QEP
BOMBAS DE LODOS
5/2/2015
332
SRL / RUBBER APPLICATION SRL / SRL-C Rubber Lined Pumps Rubber Absorbs Impact Energy from Suspended Particles due to Resilience Rubber Liners are Typically 1” Thick Larger Particles Tend to Fully Compress the Rubber and Cause Tears Sharp or Jagged Particles (Tramp Material) Tend to Tear Rubber
BOMBAS DE LODOS
333
SRL / RUBBER APPLICATION
SRL-XT Extra Thick Rubber Lined Pumps Extra Thick Rubber (up to 3X) has Higher Resilience than Conventional R-L Pumps Thicker Liners Absorb More Impact Energy Due to the Larger Size Particles in the Slurry Thicker Rubber for Longer Life
BOMBAS DE LODOS
334
SLURRY PUMP LIFE FACTORS APPLICATION POINT
BOMBAS DE LODOS
SLURRY PUMP LIFE FACTORS APPLICATION POINT - CASING
BOMBAS DE LODOS
SLURRY PUMP LIFE FACTORS APPLICATION POINT - IMPELLER
BOMBAS DE LODOS
SLURRY PUMP LIFE FACTORS APPLICATION POINT - IMPELLER
BOMBA DE LODOS
5/2/2015
338
SLURRY PUMP LIFE FACTORS APPLICATION POINT - CASING
BOMBAS DE LODOS
SLURRY PUMP LIFE FACTORS APPLICATION POINT - IMPELLER
BOMBAS DE LODOS
SLURRY PUMP LIFE FACTORS APPLICATION POINT - CASING
HIDRAULICA BASICA
5/2/2015
341
SLURRY PUMP LIFE FACTORS APPLICATION POINT - CASING
BOMBAS DE LODOS
SLURRY PUMP LIFE FACTORS APPLICATION POINT - IMPELLER
BOMBAS DE LODOS
SLURRY PUMP LIFE FACTORS APPLICATION POINT - IMPELLER
BOMBA DE LODOS
5/2/2015
344
Factor Confiabilidad para % BEP.
% BEP (% OF BEST EFF.)
LIFE FACTOR
0 TO 25
0.5
26 TO 50
0.8
51 TO 75
0.9
76 TO 100
1.0
101 TO 120
0.8
HIDRAULICA BASICA
5/2/2015
345
Desgaste por bajo flujo Mecanismo de Desgaste
BOMBA DE LODOS
5/2/2015
346
Desgaste por bajo flujo
BOMBA DE LODOS
5/2/2015
347
Desgaste por bajo flujo
BOMBA DE LODOS
5/2/2015
348
Erosion
BOMBA DE LODOS
5/2/2015
349
Erosion / Corrosion
BOMBA DE LODOS
5/2/2015
350
Erosion / Corrosion
BOMBA DE LODOS
5/2/2015
351
Erosion / Corrosion 1800 horas de uso
BOMBA DE LODOS
5/2/2015
352
Erosion / Corrosion 1500 horas de uso
BOMBA DE LODOS
5/2/2015
353
Servicios Típicos 7.1
Bombas En Serie.
7.2
Bombas en Plantas concentradoras.
7.3
Froth Pumps.
BOMBA DE LODOS
5/2/2015
354
MULTIPLE PUMPS HIGH PRESSURE PUMPS IN SERIES
Often used with Rubber-Lined Pumps to get Heads Which Exceed the Maximum Safe RPM of an Elastomer Impeller. Also Used with Metal Pumps for Slurry Pipelines. Performance Curves for all Pumps are Added. Expeller is not used on Series Services. High Pressure Pump design is often needed.
BOMBAS DE LODOS
MULTIPLE PUMPS HIGH PRESSURE MAXIMUM TDH PER STAGE
94m
65m
73m
55m
40m 70%
70%
30%
37m
BOMBAS DE LODOS
50m
40m
34m
27m
5/2/2015
356
Goulds Pumps - Slurry Pumps Coverage XHD, 5500, SRL, SRL-XT, JC Slurry Pumps
BOMBAS DE LODOS
MULTIPLE PUMPS HIGH PRESSURE NUMBER OF PUMPS PER STAGE
# OF PUMPS
=
TOTAL TDH (m) MAXIMUM TDH (m)
# OF PUMPS
=
TOTAL HP MAXIMUM HP AVAILABLE PER STATION
BOMBAS DE LODOS
5/2/2015
358
MULTIPLE PUMPS HIGH PRESSURE PUMPS IN SERIES
BOMBAS DE LODOS
PUMPS IN SERIES
BOMBAS DE LODOS
5/2/2015
360
Systems in Mineral Operations Mineral concentrate production
Complete systems Comminution circuits
Process Systems Product Systems Products
Crushing
Pumps
Grinding
Crushers
BOMBAS DE LODOS
Separation circuits
Separation
Grinding Mills Separators
Dewatering circuits
Thickening
Thickeners
Filtration
Filters
May 2, 2015
361
Planta Concentradora
BOMBAS DE LODOS
5/2/2015
362
Planta Concentradora Tamaño de Particula en Molienda
BOMBA DE LODOS
5/2/2015
363
Planta Concentradora
BOMBAS DE LODOS
5/2/2015
364
Planta Concentradora
BOMBAS DE LODOS
5/2/2015
365
Mill Circuit
BOMBAS DE LODOS
5/2/2015
366
Tratamiento de sulfuros
MINA
CHANCADO MOLIENDA FLOTACION
FeS2 H O 2
COLAS
CuFeS2 SiO2
CONC.DE Cu Y DE Mo
Al2O3
FLOT. SELECTIVA AGUA
FILTRADO Y SECADO
CONC. DE Cu SECO
FUSIÓN Y CONVERSION
CONC. DE Cu
CONC. DE Mo
REFINACION Y MOLDEO
ELECTRO REFINACIÓN CATODOS
BOMBAS DE LODOS
Proceso Productivo - Cobre
BOMBAS DE LODOS
5/2/2015
368
Diagrama de flujo del circuito de molienda flotación unitaria A FLOTACION DE PLOMO
1650 tm ps d
60%
1250 tm s pd
40%
M OL. SEC.
M OLINO
M OLINO
8x4
#1
#2
9.5X12
9.5X12
U NITAR IA
U NITARIA
CONC. Pb UNIT. 73-74%
BOMBAS DE LODOS
369
DIAGRAMA DE FLUJO DEL CIRCUITO DE FLOTACION DE PLOMO De Molinos ROUGHER Pb
SCAVENGER Pb
Relave Pb
C ELD A
MR
COLUMNA
Pb
Pb
Scv. Limpieza
1era Limpieza
2da Limpieza
Conc. Pb (cleaner)
BOMBAS DE LODOS
370
DIAGRAMA DE FLUJO DEL CIRCUITO DE FLOTACION DE ZINC RELAVE DE PLOMO
A C ON D . # 1
R O U G HER A C ON D . # 2
Zn
ROUGHER Zn
SCAVENGER Zn R EL A VE
DR-300
SCAV. LIMPIEZA SE GUNDA LI M P I E ZA
CELDA
T E RCE RA LI M P .
COLUMNA ZN
1° CL.
BOMBAS DE LODOS
SCAV. LIMPIEZA
C ON C . Z n
371
Pump Application
BOMBAS DE LODOS
5/2/2015
372
Minerales
Clasificación (de acuerdo a la naturaleza del mineral valioso que contienen)
Yacimiento nativo
El metal está en forma natural, ej. Au, Pt
Yacimiento sulfuroso
El metal está en forma de sulfuros
Yacimiento oxidado
El metal se presenta en forma de óxidos
Yacimiento complejo
BOMBAS DE LODOS
Contienen cantidades rentables de más de un mineral valioso. Ejemplo: galena y esfalerita
Trituración Por lo general se realiza en seco. Por impacto, la fragmentación se produce debido a un golpe instantáneo y seco de un material sólido duro sobre la partícula de roca o mineral, o por golpe de la partícula contra el sólido duro, o finalmente por golpes o choques entre partículas.
BOMBAS DE LODOS
Trituración Por atrición, las partículas se desmenuzan debido a fuerzas de fricción que se generan entre dos superficies duras o entre partículas. Como resultado se producen partículas bastante pequeñas o también grandes.
BOMBAS DE LODOS
Trituración Por corte, la fragmentación se produce debido a una fuerza cortante.
BOMBAS DE LODOS
Trituración Por compresión, la fragmentación se produce por acción de una fuerza de compresión generada entre dos superficies duras.
BOMBAS DE LODOS
SAG / AG Grinding Mills Servicio Clase 4
Semi-autogenous grinding mills (SAG) use a minimal ball charge in the range of 6-15% Autogenous grinding mills (AG) involves no grinding media as the ore itself is the grinding media.
Mills range in size from 18' through 40' in diameter with powers as high as 30,000 hp.
378
BOMBAS DE LODOS
5/2/2015
379
Cyclones – Servicio Clase 4
Separates materials by density using centrifugal force
– Solid/liquid – Liquid/liquid No moving parts, very reliable Many liner options to suit processes
– Hard metal – Elastomers – Ceramics Different geometries adjust performance Single units or clusters
BOMBAS DE LODOS
May 2, 2015
380
Cyclones: Terminology Underflow: Higher density material which exits via the apex Overflow: Lower density material which exits via the vortex finder
Overflow Vortex Finder
Head
Cut point/separation size/D50: The particle size at which 50% of particles exit the underflow of the cyclone Air core: Air vortex formed in the center of the cyclone, upwards from the apex. Helps with coarse solids separation. Head: Where feed enters, involute and tangent designs common
BOMBAS DE LODOS
Apex
Underflo w
May 2, 2015
381
Cyclones: Types Single:
– Some single cyclones have head diameters near 1m
Cluster:
– A group of smaller cyclones fed from a central header
– Can be individually isolated by valves for maintenance
Mozley:
– Many small cyclones inside pressure tank – Generate very high g-forces, used for slimes/fines separation
Heavy media:
– Used in coal prep to separate coal, waste rock, magnetite or ferrosilicon slurry BOMBAS DE LODOS
May 2, 2015
382
Cyclones: Performance Separation performance affected by:
– Flow rate and feed pressure – Cyclone geometry (diameters, lengths, angles, vortex finder & apex size, etc.)
– Feed properties (viscosity, solids %, liquid %) – Flow split (% to underflow, overflow) Cyclones should be running at appropriate point on performance curve
– Obtain from cyclone manufacturer or user – Gives relationship between flow, pressure drop, and separation range Pump should provide smooth, even feed to cyclone
– Proper sump design and residence time is critical – No air coring, islanding in sump
BOMBAS DE LODOS
May 2, 2015
383
Cyclones: Issues Roping
– Apex becomes choked with material instead of free flow
– Cut size becomes coarser, air core collapses Surging
– Feed surges (poor sump design, air in line, variable feed density), slurry is not delivered evenly to cyclone
– Shifts in cut point result in incorrect classification
Excessive solids in overflow
– Changes in vortex finder, operating point needed to correct problem
– Flat particles may not report to underflow despite density BOMBAS DE LODOS
May 2, 2015
384
Circuitos de Molienda (Video)
BOMBAS DE LODOS
5/2/2015
385
Flotación – Servicio Clase 2/3. Objetivo: Separar las partículas de cobre proveniente de la clasificación mediante un proceso hidrófobo, es decir introduciendo aire en celdas, y haciendo que el cobre (Ni, Mo, Zn, otros) se libere de la solución de agua y se adhiera a las burbujas de aire, logrando que el cobre concentrado flote sobre la solución. Celdas de Flotación
BOMBAS DE LODOS
Columnas de Flotación
Flotación – Servicio Clase 2/3. Factor de Espuma:
Es el porcentaje de espuma o del volumen de aire contenido en el total del volumen de una cierta solución proveniente de la flotación y otros procesos. Appication
FF
Copper Rougher Concentrate
1,5
Copper Cleaner Concentrates
3,0
Molybdenum Rougher Concentrator 2,0 Molybdenum Concentrates Iron Concentrates
Shearpeller:
Es un diseño exclusivo y patentado por ITT, para el manejo de pulpas con espumas. Se basa en alabes planos, radiales y un gran ojo de succión. Para el bombeo de Espuma sin considerar sus efectos.
BOMBAS DE LODOS
3,0 4,0 to 6,0
Flotación – Servicio Clase 2/3.
BOMBAS DE LODOS
5/2/2015
388
Flotación – Servicio Clase 2/3. FLOTACIÓN DE ESPUMA Con la flotación de espuma la separación se la realiza gracias a la adhesión selectiva de partículas hidrófobas a pequeñas burbujas de gas (aire) que son inyectadas al interior de la pulpa. El conjunto partícula-burbuja asciende a la superficie formando una espuma mineralizada, la cual es removida por medio de paletas giratorias o simplemente por rebalse. Las propiedades superficiales de las partículas y las características del medio pueden ser reguladas con ayuda de reactivos. FLOTACIÓN DE IONES Con ayuda de reactivos de flotación se precipitan los iones y luego éstos son flotados como en el caso de la flotación de espuma.
BOMBAS DE LODOS
Flotación – Servicio Clase 2/3. La flotación de espuma, es un proceso físico-químico de separación de minerales o compuestos finamente molidos, basados en las propiedades superficiales de los minerales (si son suceptibles a atrapar agua), que hace que un mineral o varios se queden en una fase o pasen a otra. Las propiedades superficiales pueden ser modificadas a voluntad con ayuda de reactivos. El proceso de flotación se basa en las propiedades hidrofílicas e hidrofóbicas de los minerales. Se trata fundamentalmente de un fenómeno de comportamiento de sólidos frente al agua Los metales nativos, sulfuros o especies como el grafito, carbón bituminoso, talco y otros son poco miscibles en agua y se llaman minerales hidrofóbicos. Por otra parte, los sulfatos, carbonatos, fosfatos, etc. Son hidrofílicos es decir son miscibles en agua. El Au, Ag, Cu, Pb, Zn, Mo, Fe, K, fosfatos, usualmente se procesan por flotación por espuma.
BOMBAS DE LODOS
Flotación – Servicio Clase 2/3. • Es la técnica que más se emplea en la concentración de minerales. • Se basa en la repelencia natural o inducida de los minerales al agua (hidrofobicidad).
BOMBAS DE LODOS
Flotación – Servicio Clase 2/3.
BOMBAS DE LODOS
5/2/2015
392
Flotación – Servicio Clase 2/3. Principales reactivos usados en la flotación de espuma COLECTOR Compuesto orgánico heteropolar que se absorbe selectivamente sobre la superficie de las partículas, haciendo que estas se vuelvan hidrófobas (aerófilas). Ejemplo: xantatos que se utilizan en la flotación de sulfuros, aceites, ditiofosfatos, sulfonatos de petroleo, otros. Una cantidad excesiva de colector haría que flotarán incluso los materiales no deseados (piritas y rocas) o los sulfuros que deberían flotar en circuitos siguientes. ACTIVADOR Compuesto inorgánico que modifica selectivamente la superficie de las partículas para permitir que el colector se absorba sobre éstas. Ejemplo: sulfato de cobre, que se utiliza en la activación de algunos sulfuros, como la antimonita.
BOMBAS DE LODOS
Flotación – Servicio Clase 2/3. Principales reactivos usados en la flotación de espuma DEPRESOR Compuesto inorgánico que modifica la superficie de las partículas volviéndolas hidrófilas o inhibe la absorción del colector. Ejemplo: sulfato de zinc, usado en la depresión de esfalerita. REGULADOR DE pH Cada sulfuro tiene su propio pH de flotación, donde puede flotar mejor. Esta propiedad varía según el mineral y su procedencia. Los reguladores de pH tienen la misión de dar a cada pulpa el pH más adecuado para una flotación óptima. La respuesta de muchos minerales para el proceso de flotación es a menudo dramáticamente afectada por el pH. Circuitos de flotación se operan usualmente a un rango de pH de 7,5 a 11,5. La cal se utiliza a menudo para elevar el pH de la pulpa y también reducir la flotación de la pirita de hierro. BOMBAS DE LODOS
Flotación – Servicio Clase 2/3. Principales reactivos usados en la flotación de espuma
ESPUMANTE Son reactivos tenso activos, que modifican la tensión superficial del agua y que producen una espuma estable. Ejemplo: Aceite de pino. Una espuma consiste de un gas disperso en un líquido en una relación tal que la densidad aparente de la mezcla se aproxima más a la densidad del gas que a la del líquido. Los productos más usados como espumante son: aceite de pino, ácido cresílico.
BOMBAS DE LODOS
Flotación – Servicio Clase 2/3. Tipos de flotación de espuma FLOTACIÓN DIRECTA La flotación directa es aquella en la que el mineral valioso sale en la espuma y la ganga se queda en el non-float. FLOTACIÓN INVERSA En este tipo de flotación el mineral valioso se queda como non-float y la ganga es la que flota. FLOTACIÓN COLECTIVA Se dice flotación colectiva en el caso de que todos los minerales valiosos y de un solo tipo mineralógico (por ejemplo: sulfuros) salen en la espuma. FLOTACIÓN SELECTIVA O DIFERENCIAL Como su nombre indica la flotación es selectiva, se flota un solo mineral a la vez en cada etapa.
BOMBAS DE LODOS
Flotación – Servicio Clase 2/3. TAMAÑO DE PARTÍCULA El tamaño de partícula a la que el mineral se muele depende de la naturaleza del mineral. La rutina debe ser lo suficientemente fina para liberar el grano mineral de roca asociada. Flotación de la espuma está generalmente limitada a las fracciones de tamaño entre unos 65 y malla 400. Las partículas mayores de 65 mallas Tyler (210 micras) son difíciles para la burbuja de aire la pueda levantar mientras que las partículas más pequeñas que 400 mallas (37 micras) a menudo no se adherirán a la burbuja de aire.
BOMBAS DE LODOS
5/2/2015
397
Flotación – Servicio Clase 2/3.
Propiedad hidrofílica e hidrofóbica de los minerales
BOMBAS DE LODOS
Flotación – Servicio Clase 2/3.
BOMBA DE LODOS
5/2/2015
399
Flotación – Servicio Clase 2/3.
BOMBA DE LODOS
5/2/2015
400
Flotación – Servicio Clase 2/3. CELDA DE FLOTACIÓN PULPA DE MINERAL PULPA DE CONCENTRADO DE COBRE
BOMBAS DE LODOS
PULPA DE MATERIAL ESTÉRIL
Flotación – Servicio Clase 2/3.
HIDRAULICA BASICA
5/2/2015
402
Flotación – Servicio Clase 2/3. CONCENTRADO DE COBRE
BOMBAS DE LODOS
Thickeners Servicio Clase 3 Up to 180m diameter Steel or concrete construction Uses gravity to separate solids with SG > liquid SG from liquid – Solids sink to bottom (underflow)
– Liquids rise to top (overflow) Includes motorized rake to prevent solids packing Discharge slurry may have >80% solids (Cw) BOMBAS DE LODOS
May 2, 2015
404
Thickened tailings pump applications (Service Class 3)
BOMBAS DE LODOS
ESPESAMIENTO Y CLARIFICACION Objetivo: Espesar los concentrados y recuperar el agua del producto. Por otro el relaves tiene la misión de: concentrar el relaves llevándolo de 35% cw a 55 cw, y recuperando agua lo más limpia posible. Espesador: Su función es concentrar un producto sin importar el remanente. Ej: Espesadores de relaves en pasta. Clarificador: Su función es sobre el overflow, dejarlo lo más limpio posible. Generalmente se colocan antes de los espesadores.
BOMBAS DE LODOS
Thickeners: Terminology Sedimentation: Processes used to gravitationally separate solids and liquids of different SGs Rake or agitator: Arm that stirs the thickened solids to prevent underflow choking Clarifier: Light duty thickeners designed for lower solids content (often used in wastewater applications) Flocculant: Chemical agent added to slurry to cause solids to form loose clumps (flocs) Mudline: Interface between settled solids and clear liquid Rake lift: Device to lift the rake when it comes into contact with settled solids – Reduces rake arm drive force, prevents arm drive damage BOMBAS DE LODOS
May 2, 2015
407
Thickeners: Types Standard
– Bridge/beam (central drive) – Traction drive – Cable drive – Column – Caisson Tray/multilevel
– Less floor space High capacity
– Injects slurry directly to bed Deep cone
– Used in some paste applications – May be rakeless BOMBAS DE LODOS
May 2, 2015
408
Flow Circuit Mineral Processing – Filter Feed (Class 2/3)
BOMBAS DE LODOS
May 2, 2015
409
ESQUEMA DE UNA PLANTA DE SULFUROS
BOMBAS DE LODOS
SRL – S Flotación - Antamina (10 Bombas)
BOMBAS DE LODOS
5/2/2015
411
5500 HP En Serie Tailings - Minera Fortuna Silver (06 Bombas)
BOMBAS DE LODOS
5/2/2015
412
5500S Underflow Clarificadores – Pierina (02 Bombas)
BOMBA DE LODOS
5/2/2015
413
5500S Underflow Clarificadores – Cajamarquilla (02 Bombas)
BOMBA DE LODOS
5/2/2015
414
5500 Alimentación a Filtro – Cajamarquilla (03 Bombas)
BOMBA DE LODOS
5/2/2015
415
SRL En Serie Tailings – Quiruvilca (03 Bombas)
BOMBA DE LODOS
5/2/2015
416
SRL Flotacion – Cajamarquilla (10 Bombas)
BOMBA DE LODOS
5/2/2015
417
Ball Mill Discharge Mines Selbais – Quebec
BOMBA DE LODOS
5/2/2015
418
Materiales 8.1
Bombas Metálicas vs Rubber.
8.2
Materiales Metálicos.
8.3
Materiales No Metálicos.
BOMBA DE LODOS
5/2/2015
419
Goulds Alloy 1228 - 25% Cr ASTM A532 Class III Type A Medium carbon-high chrome hypo-eutectic abrasion resistant iron. Primary M7C3 type carbides in a hardened martensitic matrix. Designed for severe erosive slurry services. BOMBAS DE LODOS
420
Goulds Alloy 1228 - 25% Cr Higher magnification shows primary M7C3 carbides supported in tempered martensitic matrix. Extensive secondary carbides are precipitated throughout the matrix as needles or rods of carbide for best wear resistance.
BOMBAS DE LODOS
421
Goulds Alloy 1228 - 25% Cr
Note primary carbides supported in tempered martensitic matrix. Note secondary carbides precipitated throughout the matrix in form of rods or needles.
BOMBAS DE LODOS
422
Goulds Alloy 1269 LC -30% Cr
Lower carbon- higher chrome hypo-eutectic iron of reduced carbides in mixed matrix of austenite/martensite. More chrome in matrix improves erosion and corrosion resistance in services that are more corrosive than abrasive.
BOMBAS DE LODOS
423
Goulds Alloy 1650 HC -35% Cr Ferritic irons develop with very high chrome levels, offering superior erosioncorrosion resistance. Designed for erosive slurry services that are also highly corrosive. Matrix is ferritic with spheroidized carbides distributed uniformly for superior corrosion and erosion resistance. BOMBAS DE LODOS
424
Goulds 1216 CD-4MCuN ASTM A890 Grade CD4MCuN
Duplex stainless consists of isolated pools of austenite in a ferrite matrix. Typical Brinell hardness of 220-270 HB. Can be age hardened to 325 HB. Used in erosive/corrosive chemical services. BOMBAS DE LODOS
425
Material Application Guidelines
Alloy Type
Brinell Hardness
pH
Application
25% Chrome Iron
550-650
4.5-12
Heavy slurry, 15% hard solids Mild-Corrosive; Highly Abrasive Best Abrasion Resistance
450-550
4-12.5
Heavy slurry, 15% hard solids More-Corrosive; Less-Erosive Better Corrosion Resistance and Toughness – Low Carbon
450-550
2-13
Heavy slurry, 15% hard solids More-Corrosive; Erosive services Superior Erosion-Corrosion
(1228) Martensitic ASTM A532 Class III Type A
30% Chrome Iron (1269) Mix Aust-Mart No ASTM
35% Chrome Iron (1650) Ferritic No ASTM
BOMBAS DE LODOS
426
Material Application Guidelines
BOMBAS DE LODOS
5/2/2015
427
Application – Elastomer Selection Hardness
Elastomer Type
Durometer
Maximum
Shore A
Resistance to
pH
Temperature
Min.
Max.
Abrasion
Moderate Chemicals
Hydrocarbons
& Oils
Natural Rubber
40
154 oF
68 oC
4.5
12
E
G(1)
P
Natural Rubber (Soft)
36
150 oF
66 oC
4.5
12
E
G(1)
P
Natural Rubber (Hard)
50
180 oF
82 oC
4.5
12
E
G(1)
P
Neoprene
60
212 oF
100 oC
3.0
12
G
G(1)
G
Nitrile (60)
60
220 oF
105 oC
3.5
12
G
G(1)
E
Chlorobutyl
50
250 oF
121 oC
1.0
12
G
E
P
Hypalon®
55
230 oF
110 oC
View more...
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