Respiratory Gas Exchange in the Lungs
Total Page:16
File Type:pdf, Size:1020Kb
Load more
Recommended publications
-
Solutes and Solution
Solutes and Solution The first rule of solubility is “likes dissolve likes” Polar or ionic substances are soluble in polar solvents Non-polar substances are soluble in non- polar solvents Solutes and Solution There must be a reason why a substance is soluble in a solvent: either the solution process lowers the overall enthalpy of the system (Hrxn < 0) Or the solution process increases the overall entropy of the system (Srxn > 0) Entropy is a measure of the amount of disorder in a system—entropy must increase for any spontaneous change 1 Solutes and Solution The forces that drive the dissolution of a solute usually involve both enthalpy and entropy terms Hsoln < 0 for most species The creation of a solution takes a more ordered system (solid phase or pure liquid phase) and makes more disordered system (solute molecules are more randomly distributed throughout the solution) Saturation and Equilibrium If we have enough solute available, a solution can become saturated—the point when no more solute may be accepted into the solvent Saturation indicates an equilibrium between the pure solute and solvent and the solution solute + solvent solution KC 2 Saturation and Equilibrium solute + solvent solution KC The magnitude of KC indicates how soluble a solute is in that particular solvent If KC is large, the solute is very soluble If KC is small, the solute is only slightly soluble Saturation and Equilibrium Examples: + - NaCl(s) + H2O(l) Na (aq) + Cl (aq) KC = 37.3 A saturated solution of NaCl has a [Na+] = 6.11 M and [Cl-] = -
Gas Exchange
Gas exchange Gas exchange occurs as a result of respiration, when carbon dioxide is excreted and oxygen taken up, and photosynthesis, when oxygen is excreted and carbon dioxide is taken up. The rate of gas exchange is affected by: • the area available for diffusion • the distance over which diffusion occurs • the concentration gradient across the gas exchange surface • the speed with which molecules diffuse through membranes. Efficient gas exchange systems must: • have a large surface area to volume ratio • be thin • have mechanisms for maintaining steep concentration gradients across themselves • be permeable to gases. Single-celled organisms are aquatic and their cell surface membrane has a sufficiently large surface area to volume ratio to act as an efficient gas exchange surface. In larger organisms, permeable, thin, flat structures have all the properties of efficient gas exchange surfaces but need water to prevent their dehydration and give them mechanical support. Since the solubility of oxygen in water is low, organisms that obtain their oxygen from water can maintain only a low metabolic rate. In small and thin organisms, the distance from gas exchange surface to the inside of the organism is short enough for diffusion of gases to be efficient. Diffusion gradients are maintained because gases are continually used up or produced. In larger organisms, simple diffusion is not an efficient way of transporting gases between cells in the body and the gas exchange surface. In many animals a blood circulatory system carries gases to and from the gas exchange surface. The gas-carrying capacity of the blood is increased by respiratory pigments, such as haemoglobin. -
Mechanisms of Pulmonary Gas Exchange Abnormalities During Experimental Group B Streptococcal Infusion
003 I -3998/85/1909-0922$02.00/0 PEDIATRIC RESEARCH Vol. 19, No. 9, I985 Copyright 0 1985 International Pediatric Research Foundation, Inc. Printed in (I.S. A. Mechanisms of Pulmonary Gas Exchange Abnormalities during Experimental Group B Streptococcal Infusion GREGORY K. SORENSEN, GREGORY J. REDDING, AND WILLIAM E. TRUOG ABSTRACT. Group B streptococcal sepsis in newborns obtained from GBS (5, 6). Arterial Poz fell by 9 torr in association produces pulmonary arterial hypertension and hypoxemia. with the increase in pulmonary arterial pressure (4). In contrast, The purpose of this study was to investigate the mecha- the neonatal piglet infused with GBS demonstrated both pul- nisms by which hypoxemia occurs. Ten anesthetized, ven- monary arterial hypertension and profound arterial hypoxemia tilated piglets were infused with 2 x lo9 colony forming (7). These results suggest that the neonatal pulmonary vascula- unitstkg of Group B streptococci over a 30-min period. ture may respond to bacteremia differently from that of adults. Pulmonary arterial pressure rose from 14 ? 2.8 to 38 ? The relationship between Ppa and the matching of alveolar 6.7 torr after 20 min of the bacterial infusion (p< 0.01). ventilation and pulmonary perfusion, a major determinant of During the same period, cardiac output fell from 295 to arterial oxygenation during room air breathing (8), has not been 184 ml/kg/min (p< 0.02). Arterial Po2 declined from 97 studied in newborns. The predictable rise in Ppa with an infusion 2 7 to 56 2 11 torr (p< 0.02) and mixed venous Po2 fell of group B streptococcus offers an opportunity to delineate the from 39.6 2 5 to 28 2 8 torr (p< 0.05). -
Page 1 of 6 This Is Henry's Law. It Says That at Equilibrium the Ratio of Dissolved NH3 to the Partial Pressure of NH3 Gas In
CHMY 361 HANDOUT#6 October 28, 2012 HOMEWORK #4 Key Was due Friday, Oct. 26 1. Using only data from Table A5, what is the boiling point of water deep in a mine that is so far below sea level that the atmospheric pressure is 1.17 atm? 0 ΔH vap = +44.02 kJ/mol H20(l) --> H2O(g) Q= PH2O /XH2O = K, at ⎛ P2 ⎞ ⎛ K 2 ⎞ ΔH vap ⎛ 1 1 ⎞ ln⎜ ⎟ = ln⎜ ⎟ − ⎜ − ⎟ equilibrium, i.e., the Vapor Pressure ⎝ P1 ⎠ ⎝ K1 ⎠ R ⎝ T2 T1 ⎠ for the pure liquid. ⎛1.17 ⎞ 44,020 ⎛ 1 1 ⎞ ln⎜ ⎟ = − ⎜ − ⎟ = 1 8.3145 ⎜ T 373 ⎟ ⎝ ⎠ ⎝ 2 ⎠ ⎡1.17⎤ − 8.3145ln 1 ⎢ 1 ⎥ 1 = ⎣ ⎦ + = .002651 T2 44,020 373 T2 = 377 2. From table A5, calculate the Henry’s Law constant (i.e., equilibrium constant) for dissolving of NH3(g) in water at 298 K and 340 K. It should have units of Matm-1;What would it be in atm per mole fraction, as in Table 5.1 at 298 K? o For NH3(g) ----> NH3(aq) ΔG = -26.5 - (-16.45) = -10.05 kJ/mol ΔG0 − [NH (aq)] K = e RT = 0.0173 = 3 This is Henry’s Law. It says that at equilibrium the ratio of dissolved P NH3 NH3 to the partial pressure of NH3 gas in contact with the liquid is a constant = 0.0173 (Henry’s Law Constant). This also says [NH3(aq)] =0.0173PNH3 or -1 PNH3 = 0.0173 [NH3(aq)] = 57.8 atm/M x [NH3(aq)] The latter form is like Table 5.1 except it has NH3 concentration in M instead of XNH3. -
THE SOLUBILITY of GASES in LIQUIDS Introductory Information C
THE SOLUBILITY OF GASES IN LIQUIDS Introductory Information C. L. Young, R. Battino, and H. L. Clever INTRODUCTION The Solubility Data Project aims to make a comprehensive search of the literature for data on the solubility of gases, liquids and solids in liquids. Data of suitable accuracy are compiled into data sheets set out in a uniform format. The data for each system are evaluated and where data of sufficient accuracy are available values are recommended and in some cases a smoothing equation is given to represent the variation of solubility with pressure and/or temperature. A text giving an evaluation and recommended values and the compiled data sheets are published on consecutive pages. The following paper by E. Wilhelm gives a rigorous thermodynamic treatment on the solubility of gases in liquids. DEFINITION OF GAS SOLUBILITY The distinction between vapor-liquid equilibria and the solubility of gases in liquids is arbitrary. It is generally accepted that the equilibrium set up at 300K between a typical gas such as argon and a liquid such as water is gas-liquid solubility whereas the equilibrium set up between hexane and cyclohexane at 350K is an example of vapor-liquid equilibrium. However, the distinction between gas-liquid solubility and vapor-liquid equilibrium is often not so clear. The equilibria set up between methane and propane above the critical temperature of methane and below the criti cal temperature of propane may be classed as vapor-liquid equilibrium or as gas-liquid solubility depending on the particular range of pressure considered and the particular worker concerned. -
Producing Nitrogen Via Pressure Swing Adsorption
Reactions and Separations Producing Nitrogen via Pressure Swing Adsorption Svetlana Ivanova Pressure swing adsorption (PSA) can be a Robert Lewis Air Products cost-effective method of onsite nitrogen generation for a wide range of purity and flow requirements. itrogen gas is a staple of the chemical industry. effective, and convenient for chemical processors. Multiple Because it is an inert gas, nitrogen is suitable for a nitrogen technologies and supply modes now exist to meet a Nwide range of applications covering various aspects range of specifications, including purity, usage pattern, por- of chemical manufacturing, processing, handling, and tability, footprint, and power consumption. Choosing among shipping. Due to its low reactivity, nitrogen is an excellent supply options can be a challenge. Onsite nitrogen genera- blanketing and purging gas that can be used to protect valu- tors, such as pressure swing adsorption (PSA) or membrane able products from harmful contaminants. It also enables the systems, can be more cost-effective than traditional cryo- safe storage and use of flammable compounds, and can help genic distillation or stored liquid nitrogen, particularly if an prevent combustible dust explosions. Nitrogen gas can be extremely high purity (e.g., 99.9999%) is not required. used to remove contaminants from process streams through methods such as stripping and sparging. Generating nitrogen gas Because of the widespread and growing use of nitrogen Industrial nitrogen gas can be produced by either in the chemical process industries (CPI), industrial gas com- cryogenic fractional distillation of liquefied air, or separa- panies have been continually improving methods of nitrogen tion of gaseous air using adsorption or permeation. -
Oxygenation and Oxygen Therapy
Rules on Oxygen Therapy: Physiology: 1. PO2, SaO2, CaO2 are all related but different. 2. PaO2 is a sensitive and non-specific indicator of the lungs’ ability to exchange gases with the atmosphere. 3. FIO2 is the same at all altitudes 4. Normal PaO2 decreases with age 5. The body does not store oxygen Therapy & Diagnosis: 1. Supplemental O2 is an FIO2 > 21% and is a drug. 2. A reduced PaO2 is a non-specific finding. 3. A normal PaO2 and alveolar-arterial PO2 difference (A-a gradient) do NOT rule out pulmonary embolism. 4. High FIO2 doesn’t affect COPD hypoxic drive 5. A given liter flow rate of nasal O2 does not equal any specific FIO2. 6. Face masks cannot deliver 100% oxygen unless there is a tight seal. 7. No need to humidify if flow of 4 LPM or less Indications for Oxygen Therapy: 1. Hypoxemia 2. Increased work of breathing 3. Increased myocardial work 4. Pulmonary hypertension Delivery Devices: 1. Nasal Cannula a. 1 – 6 LPM b. FIO2 0.24 – 0.44 (approx 4% per liter flow) c. FIO2 decreases as Ve increases 2. Simple Mask a. 5 – 8 LPM b. FIO2 0.35 – 0.55 (approx 4% per liter flow) c. Minimum flow 5 LPM to flush CO2 from mask 3. Venturi Mask a. Variable LPM b. FIO2 0.24 – 0.50 c. Flow and corresponding FIO2 varies by manufacturer 4. Partial Rebreather a. 6 – 10 LPM b. FIO2 0.50 – 0.70 c. Flow must be sufficient to keep reservoir bag from deflating upon inspiration 5. -
Part Two Physical Processes in Oceanography
Part Two Physical Processes in Oceanography 8 8.1 Introduction Small-Scale Forty years ago, the detailed physical mechanisms re- Mixing Processes sponsible for the mixing of heat, salt, and other prop- erties in the ocean had hardly been considered. Using profiles obtained from water-bottle measurements, and J. S. Turner their variations in time and space, it was deduced that mixing must be taking place at rates much greater than could be accounted for by molecular diffusion. It was taken for granted that the ocean (because of its large scale) must be everywhere turbulent, and this was sup- ported by the observation that the major constituents are reasonably well mixed. It seemed a natural step to define eddy viscosities and eddy conductivities, or mix- ing coefficients, to relate the deduced fluxes of mo- mentum or heat (or salt) to the mean smoothed gra- dients of corresponding properties. Extensive tables of these mixing coefficients, KM for momentum, KH for heat, and Ks for salinity, and their variation with po- sition and other parameters, were published about that time [see, e.g., Sverdrup, Johnson, and Fleming (1942, p. 482)]. Much mathematical modeling of oceanic flows on various scales was (and still is) based on simple assumptions about the eddy viscosity, which is often taken to have a constant value, chosen to give the best agreement with the observations. This approach to the theory is well summarized in Proudman (1953), and more recent extensions of the method are described in the conference proceedings edited by Nihoul 1975). Though the preoccupation with finding numerical values of these parameters was not in retrospect always helpful, certain features of those results contained the seeds of many later developments in this subject. -
THE SOLUBILITY of GASES in LIQUIDS INTRODUCTION the Solubility Data Project Aims to Make a Comprehensive Search of the Lit- Erat
THE SOLUBILITY OF GASES IN LIQUIDS R. Battino, H. L. Clever and C. L. Young INTRODUCTION The Solubility Data Project aims to make a comprehensive search of the lit erature for data on the solubility of gases, liquids and solids in liquids. Data of suitable accuracy are compiled into data sheets set out in a uni form format. The data for each system are evaluated and where data of suf ficient accuracy are available values recommended and in some cases a smoothing equation suggested to represent the variation of solubility with pressure and/or temperature. A text giving an evaluation and recommended values and the compiled data sheets are pUblished on consecutive pages. DEFINITION OF GAS SOLUBILITY The distinction between vapor-liquid equilibria and the solUbility of gases in liquids is arbitrary. It is generally accepted that the equilibrium set up at 300K between a typical gas such as argon and a liquid such as water is gas liquid solubility whereas the equilibrium set up between hexane and cyclohexane at 350K is an example of vapor-liquid equilibrium. However, the distinction between gas-liquid solUbility and vapor-liquid equilibrium is often not so clear. The equilibria set up between methane and propane above the critical temperature of methane and below the critical temperature of propane may be classed as vapor-liquid equilibrium or as gas-liquid solu bility depending on the particular range of pressure considered and the par ticular worker concerned. The difficulty partly stems from our inability to rigorously distinguish between a gas, a vapor, and a liquid, which has been discussed in numerous textbooks. -
Gas-Liquid Hollow Fiber Membrane Contactors for Different Applications
Review Gas-Liquid Hollow Fiber Membrane Contactors for Different Applications Stepan D. Bazhenov 1,*, Alexandr V. Bildyukevich 2 and Alexey V. Volkov 1 1 A.V. Topchiev Institute of Petrochemical Synthesis, Russian Academy of Sciences, Moscow 119991, Russia; [email protected] 2 Institute of Physical Organic Chemistry, National Academy of Sciences of Belarus, Minsk 220072, Belarus; [email protected] * Correspondence: [email protected]; Tel.: +7-495-647-5927 (ext. 202) Received: 14 September 2018; Accepted: 2 October 2018; Published: 10 October 2018 Abstract: Gas-liquid membrane contactors that were based on hollow fiber membranes are the example of highly effective hybrid separation processes in the field of membrane technology. Membranes provide a fixed and well-determined interface for gas/liquid mass transfer without dispensing one phase into another while their structure (hollow fiber) offers very large surface area per apparatus volume resulted in the compactness and modularity of separation equipment. In many cases, stated benefits are complemented with high separation selectivity typical for absorption technology. Since hollow fiber membrane contactors are agreed to be one of the most perspective methods for CO2 capture technologies, the major reviews are devoted to research activities within this field. This review is focused on the research works carried out so far on the applications of membrane contactors for other gas-liquid separation tasks, such as water deoxygenation/ozonation, air humidity control, ethylene/ethane separation, etc. A wide range of materials, membranes, and liquid solvents for membrane contactor processes are considered. Special attention is given to current studies on the capture of acid gases (H2S, SO2) from different mixtures. -
Respiratory Therapy Pocket Reference
Pulmonary Physiology Volume Control Pressure Control Pressure Support Respiratory Therapy “AC” Assist Control; AC-VC, ~CMV (controlled mandatory Measure of static lung compliance. If in AC-VC, perform a.k.a. a.k.a. AC-PC; Assist Control Pressure Control; ~CMV-PC a.k.a PS (~BiPAP). Spontaneous: Pressure-present inspiratory pause (when there is no flow, there is no effect ventilation = all modes with RR and fixed Ti) PPlateau of Resistance; Pplat@Palv); or set Pause Time ~0.5s; RR, Pinsp, PEEP, FiO2, Flow Trigger, rise time, I:E (set Pocket Reference RR, Vt, PEEP, FiO2, Flow Trigger, Flow pattern, I:E (either Settings Pinsp, PEEP, FiO2, Flow Trigger, Rise time Target: < 30, Optimal: ~ 25 Settings directly or by inspiratory time Ti) Settings directly or via peak flow, Ti settings) Decreasing Ramp (potentially more physiologic) PIP: Total inspiratory work by vent; Reflects resistance & - Decreasing Ramp (potentially more physiologic) Card design by Respiratory care providers from: Square wave/constant vs Decreasing Ramp (potentially Flow Determined by: 1) PS level, 2) R, Rise Time ( rise time ® PPeak inspiratory compliance; Normal ~20 cmH20 (@8cc/kg and adult ETT); - Peak Flow determined by 1) Pinsp level, 2) R, 3)Ti (shorter Flow more physiologic) ¯ peak flow and 3.) pt effort Resp failure 30-40 (low VT use); Concern if >40. Flow = more flow), 4) pressure rise time (¯ Rise Time ® Peak v 0.9 Flow), 5) pt effort ( effort ® peak flow) Pplat-PEEP: tidal stress (lung injury & mortality risk). Target Determined by set RR, Vt, & Flow Pattern (i.e. for any set I:E Determined by patient effort & flow termination (“Esens” – PDriving peak flow, Square (¯ Ti) & Ramp ( Ti); Normal Ti: 1-1.5s; see below “Breath Termination”) < 15 cmH2O. -
Gas Exchange in the Prone Posture
RESPIRATORY CARE Paper in Press. Published on May 30, 2017 as DOI: 10.4187/respcare.05512 Gas Exchange in the Prone Posture Nicholas J Johnson MD, Andrew M Luks MD, and Robb W Glenny MD Introduction Overview of Gas Exchange Lung Structure Normal Exchange of Oxygen and Carbon Dioxide Abnormal Exchange of Oxygen and Carbon Dioxide Gas Exchange in the Prone Posture Under Normal Conditions Spatial Distribution of Ventilation Spatial Distribution of Perfusion Ventilation and Perfusion Matching Mechanisms by Which the Prone Posture Improves Gas Exchange in Animal Models of ARDS Additional Physiologic Effects of the Prone Posture Clinical Trials Summary The prone posture is known to have numerous effects on gas exchange, both under normal condi- tions and in patients with ARDS. Clinical studies have consistently demonstrated improvements in oxygenation, and a multi-center randomized trial found that, when implemented within 48 h of moderate-to-severe ARDS, placing subjects in the prone posture decreased mortality. Improve- ments in gas exchange occur via several mechanisms: alterations in the distribution of alveolar ventilation, redistribution of blood flow, improved matching of local ventilation and perfusion, and reduction in regions of low ventilation/perfusion ratios. Ventilation heterogeneity is reduced in the prone posture due to more uniform alveolar size secondary to a more uniform vertical pleural pressure gradient. The prone posture results in more uniform pulmonary blood flow when com- pared with the supine posture, due to an anatomical bias for greater blood flow to dorsal lung regions. Because both ventilation and perfusion heterogeneity decrease in the prone posture, gas exchange improves.