Ultrafiltration in PD: Physiologic Principles



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Ultrafiltration in PD: Physiologic Principles Ali K. Abu-Alfa, MD, FASN Professor of Medicine Head, Division of Nephrology and Hypertension American University of Beirut Beirut, Lebanon Adjunct Faculty Section of Nephrology Yale School of Medicine New Haven, CT Version Date: February 2012

DISCLOSURES Dr Abu-Alfa has served as a Consultant for Baxter Healthcare, and has received research grants and honoraria for speaking engagements and/or organization of PD educational conferences from Baxter Healthcare. Dr Abu-Alfa is the immediate past co-president for the North American Chapter of the International Society for Peritoneal Dialysis. 2

Educational Objectives Review physiologic basis of ultrafiltration Review the impact of membrane transport characteristics in UF volume. Compare osmotic and oncotic forces and effect on UF. Discuss Na sieveing and Na removal. Review membrane changes over time. 3

Mechanisms at Play Trans-capillary fluid movement: Osmotic / Oncotic gradient (first and foremost). Hydrostatic pressure (much less so). Membrane function / surface area. Lymphatic re-absorption. 4

Structure of Peritoneal Membrane 5

Normal Human Peritoneum RBCs Endothelium Interstitium Mesothelium Adapted from Lai et al: J Am Soc Nephrol 12: 1036 1045, 2001 6

Structure of Peritoneal Membrane H 2 O Capillary Peritoneal Space Glucose Aquaporin mediated: 50% Intercellular: 50% Glucose transporter mediated: minimal Intercellular: >90% 7

Sodium Sieving with 4.25% Glucose LaMilia et al, Nephrol Dial Transplant (2004) 19: 1849-1855 8

Role of Aquaporins: Aqp1 -/- mouse AQP: V(t): UF: Aquaporin Volume versus time Ultrafiltration Ni J et al: Kidney International (2006) 69, 1518 1525 9

Three-pore model = Osmotic P = Hydraulic r = Radius Rippe et al: Microcirculation 8, 303 320, 2001 10

Small Pores and Aquaporins 4.25% LaMilia et al, Kidney Int 72:643-50, 2007 PET: Peritoneal Equilibration test 11

Crystalloid Osmosis Normal serum osmolality = 270 mosm/l Uremic serum osmolality = 305 mosm/l Dialysate Glucose mosm/l 1.5 % 345 2.5 % 395 4.25 % 484 12

UF with 4.25% Glucose: Small Pores Hydrostatic (mmhg) Colloid (mmhg) Osmolality (mosm/kg H 2 O) Crystalloid (mmhg) Capillary Pressure Dialysate Pressure Pressure Gradient 17 12-18 0-6 26 0.1-26 305 (Glu) 486 - - 105 Van t Hoff Law: Osmolar gradient * 19.3 * reflection coefficient (0.03) Krediet R et al: Peritoneal Dialysis International 1997: 17, 35-41 13

UF with 4.25% Glucose: Aquaporins Hydrostatic (mmhg) Colloid (mmhg) Osmolality (mosm/kg H 2 O) Capillary Pressure Dialysate Pressure Pressure Gradient 17 12-18 0-6 26 0.1-26 305 486 Crystalloid (mmhg) Across Small pores Across Aquaporins 105 3559 Van t Hoff Law: Osmolar gradient * 19.3 * reflection coefficient (0.03) Krediet R et al: Peritoneal Dialysis International 1997: 17, 35-41 14

Sodium Sieving and Na Removal 250 200 150 100 CAPD APD Icodextrin 50 0 Na removal meq Rodriguez-Carmona, PDI 2003 (22): 705-713. 15

Glucose Absorption and UF Profile Intraperitoneal glucose amount, % of initial 100 8 0 60 40 2 0 4.25 % (n=23) 2.5 % (n=9) 1.5 % (n=9) 0 100 0 60 120 180 240 300 360 0 2 0 40 60 80 Amount of glucose absorbed % of initial intraperitoneal amount 4.25 % Glucose Time, min Heimbürger et al. Kidney Int 1992: 41: 1320-32 Krediet R et al: Peritoneal Dialysis International 1997: 17, 35-41 16

Net Ultrafiltration Profile Absorption Transcapillary UF Net UF Cumulative transport (ml) 800 600 400 200 0-200 -400-600 -30 0 30 60 90 120 150 180 210 240 Time (min) Adapted from Mactier RA, et al. J Clin Invest. 1987;80:1311-1316. 17 UF: Ultrafiltration

Variables to Consider Effect of dwell time Effect of fill volume Effect of membrane transport profile Effect of larger molecules 18

Effect of Fill Volume: Net UF Volume 400 350 300 UF ml 250 200 150 100 50 0 2000 2500 3000 Dwell Volume, 2.5% Glucose, 4 hours Abu-Alfa, American Society of Nephrology, Abstract 2001 19

Glucose Kinetics by Transport Status D/D0 Glucose 1 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2 D/P: Dialysate / Plasma 0 1 2 3 4 Hours L LA HA H L: Low Transporter LA: Low Average Transporter HA: High Average Transporter H: High Transporter 20

Crystalloid versus colloid osmosis Blood in Peritoneal Capillaries Endothelium urea creatinine macromolecules glucose crystalloid osmosis osmosis colloid Mesothelium Dialysate filled Peritoneal Cavity Adapted from Krediet R et al: Peritoneal Dialysis International 17, 35-41; 1997 21

Colloid Osmosis: Source and Structure of Icodextrin Corn Starch Enzymatic hydrolysis Membrane fractionation Malto-Dextrin Icodextrin 22

UF with 7.5% Icodextrin Hydrostatic (mmhg) Colloid (mmhg) Osmolality (mosm/kg H 2 O) Crystalloid (mmhg) Capillary Pressure Dialysate Pressure Pressure Gradient 17 12-18 0-6 26 66 40 305 285 - - 12 Van t Hoff Law: Osmolar gradient * 19.3 * reflection coefficient (0.03) Krediet R et al: Peritoneal Dialysis International 1997: 17, 35-41 23

Transport Status and Icodextrin Krediet R et al: Peritoneal Dialysis International 1997: 17, 35-41 TCUFR: Transcapillary UF rate MTAC: Mean Transport Area Coefficient 24

Transport Status: Icodextrin vs 2.5% D/P: ICO: GLU: Cr: Dialysate/Plasma Icodextrin Glucose Creatinine Lin A et al: Clin J Am Soc Nephrol 2009: 4: 1799 1804 25

Glucose absorption: Caloric Cost Glucose absorbed (g/8 hrs) 90 80 70 60 50 40 30 20 10 0 Widening differential 1.50% 2.50% 4.25% Low Low Ave. High Ave. High Peritoneal Transport Type Courtesy of Dr Salim Mujais, Baxter Healthcare 2002 26

Changes in Transport Profile Glucose exposure (grams/year) 70000 60000 50000 40000 30000 Year 1 Year 2 Year 3 Year 4 Year 5 Time on Treatment Group 1 Group 2 Solute Transport (D/P creatinine at 4 hours 0.8 0.75 0.7 0.65 0.6 0.55 0.5 Start Year 1 Year 2 Year 3 Year 4 Year 5 Group 1 Group 2 Davies et al. J Am Soc Nephrol. 2001;12:1046-51 27

Physiologic Principles for UF in PD Summary UF in PD is primarily driven by osmotic (Glucose) or oncotic (icodextrin) forces across the membrane. Sodium sieving is maximal at about 60 90 minutes of a dwell, and will result in and decreased Na concentration in the dialysate if dwell is drained, as with cyclic PD. Na sieving negatively impacts total Na removed. Many factors modulate UF volume such as glucose concentration, dwell time, dwell volume and intrinsic membrane transport type of each patient. Higher transport rates result in less UF with glucose solutions but not with icodextrin solution. 28

Question 1 The removal of sodium with PD is dependent on convection and diffusion. Calculate the approximate amount of Na removed during a dwell for each of the following conditions: 1) No net ultrafiltration after a 4 hours dwell using 2 liters of 2.5% dextrose solution with [Na]=132 meq/l and plasma [Na]=140 meq/l. 2) 500 cc of net ultrafiltration after a 10 hours dwell using 2 liters of 7.5% icodextrin solution with [Na]=132 meq/l and plasma [Na]=140 meq/l. 3) 250 cc of net UF after a 1 hour dwell using 2 liters of 2.5% dextrose solution with [Na]=132 meq/l and 60 mins dialysate [Na]=128 meq/l, with a short APD cycle. 29

Answer 1 The removal of sodium with PD is dependent on convection and diffusion. Calculate the approximate amount of Na removed during a dwell for each of the following conditions: 1) No net ultrafiltration after a 4 hours dwell using 2 liters of 2.5% dextrose solution with [Na]=132 meq/l and plasma [Na]=140 meq/l. Answer: 16 meq 2) 500 cc of net ultrafiltration after a 10 hours dwell using 2 liters of 7.5% icodextrin solution with [Na]=132 meq/l and plasma [Na]=140 meq/l. Answer: 16+70=86 meq 3) 250 cc of net UF after a 1 hour dwell using 2 liters of 2.5% dextrose solution with [Na]=132 meq/l and 60 mins dialysate [Na]=128 meq/l, with a short APD cycle.. Answer: 24 meq 30