COLLOID PROPULSION METHOD and APPARATUS Flled March 12, 1963

Total Page:16

File Type:pdf, Size:1020Kb

COLLOID PROPULSION METHOD and APPARATUS Flled March 12, 1963 6.T. NORGREN COLLOID PROPULSION METHOD AND APPARATUS FLled March 12, 1963 FIG. I FIG. 2 ~NV~NTOR~ CARL T. NORGREN 1 are charged at the nozzle exhaust by any convenient 3,173,246 means, such as a corona discharge. The resulting padi- COLLOID PROPULSION METHOD AND APPARATUS cles are then accelerafed by suitable means such as an Carl T. Norgren, North Olmsted, Ohio, electrostatic accelerator. It is likewise contemplated that United States of America as repre [i the colloidal particles can be charged in an electron bom- Administrator of the National Aeronautics and Space bardment engine and then accelerated. In an alternate Administration embodiment of the invention the colloidal particles are Filed Mar. 12,1963, Ser. No. 264,735 accelerated in the nozzle alone to supply small corrections 10 Claims. (C1.60-35.3) to planned orbits. (Granted under Title 35, Code (19521, sec. 266) US. 10 It is, therefore, an object of the present invention to The invention described herein may be manufactured provide an improved method of propulsion in which sub- and used by or for the Government of the United States micron sized particles are utilized which enables realistic of America for governmental purposes without the pay- accelerating potentials to be used. ment of any royalties thereon or therefor. Another object to the invention is provide an improved This invention is concerned with a method and appara- 15 thrustor which utilizes a colloidal particle generator tus for propelling space vehicles, and more particularly having a supersonic nozzle. with an onboard colloidal particle generator for an elec- Other objects of the invention will be apparent from tro static engine. The invention is especially concerned the specification which follows and from the drawings with an improved thrustor which utilizes a colloidal par- in which like numerals are used throughout to identify ticle generator. 20 likeparts. Colloidal particle electrostatic rocket engines have been FIG. 1 is a schematic view of an electrostatic engine proposed as propulsion systems for space missions where having a thrustor constructed in accordance with the in- specific impulses from 1,000 to 10,000 seconds are re- vention, and FIG 2 is a perspective view of a colloid quired. High power efficiency, high propellant utiliza- particle generator of the invention. tion, reasonable field strengths, physical and electrical 25 Referring now to the drawings there is shown in FIG. 1 reliability, light weight, and long-duration operation are an electrostatic engine 10 for rockets and the like that all required of these engines. may be used with electric spacecraft. The electrostatic Various methods have been used to form colloidal engine 10 comprises a power supply 12 and a thrustor 14. particles such as expanding material into a cooling or The power supply 12 may be any of a number of different calming chamber through a high presscre nozzle. Chem- 30 types such as a nuclear reactor that is used to drive a ical reactions such as the action of ammonia vapor in turbine or a nuclear battery. hydrogen chloride have likewise been utilized along with The thrustor 14 comprises a propellent vaporizer 16. the oxidation of a particle forming material. Colloidal a supersonic nozzle 18, charging means 20, and accel- particles have also been produced by physical grinding erators 22 and 24. An electron trap 26 is provided where such as mechanical disintegration in a colloidal mill. 35 the vaporizer 16 and the nozzle 18 are operated at ground These techniques have disadvantages when applied to potential to prevent the back streaming of electrons from propulsion systems. For example, the atomization of a the charging means 20. material, such as a liquid, 'tends to produce a very poor The vaporizer 16 and the nozzle 18 compnse a colloidal size distribution which is completely unsuitable for an particle generator which is indirectly heated in a con- electrostatic engine. Other devices which provide good 40 ventional manner for supplying sub-micron sized particles size distribution of the particles do not produce a suffi- to be charged and accelerated. By way of example, an cient quantity of particles to be useful. Also methods A.C.' Nichrome heating unit 28 wound around the va- which produce relatively uniform prepared particles porizer 16 and a similar heating unit 30 wound around often require a carrier, and it can be quite difficult to [he nozzle 18 have been successfully used. Heat shields separate the particles from the carrier. Moreover, even 4.j 32 and 34 are provided to reduce radiation heat losses. when the particles are separated from the carrier they The heating units 28 and 30 are connected to an auxiliary tend to form aggregates which are very difficult to sepa- power supply 36 and the entire colloidal particle genera- rate. tor is maintained at a zero potential with respect to These problems have been solved by the present in- ground. vention which utilizes the condensation of a homogenous 50 In operation, a supply of propellent is enclosed in the vapor in a supersonic nozzle to obtain sub-micron sized vaporizer 16 and heated by the heating unit 28 to form colloidal particles. In this manner vaporization, nuclea- a homogenous vapor which is then expanded in the nozzle tion, condensation, aggregation and possible revaporiza- 18 to form sub-micron sized colloidal particles. The tion occur at an extremely rapid rate, on the order of heating unit 30 prevents condensation of these particles one millisecond. According to the present invention 5.j on the nozzle surface. a material is vaporized and then passed through a con- The particle formation on a nozzle condensation prw- vergent-divergent nozzle wherein adiabatic expansion ess is highly complex, and is dependent primarily on of the vapor produces the required supersaturation for reaching a critical nucleation rate in the vapor flow. particle growth. The collision rate of the particles is This rate is a function of the supersaturation, tempera- controlled by the physical properties of the vapor as well GO ture, and physical properties of the propellent in the as the dimensions of the apparatus, and in this manner the vapor stream. particle growth rate and size is controlled so that the Supersaturation is controlled by the flow rate in the particles have atomic mass units (a.m.u.'s) that are nar- nozzle 18. Because the nozzle throat functions as a critical flow orifice, the vapor pressure of the propellent rowly distributed in a predetermined mass range. The system is operated at a maximum pressure determined 6.j in the vaporizer 16 must be high enough so that adiabatic expansion can occur in the nozzle 18. This expansion by the vapor pressure of the material; consequently the creates the necessary conditions for the supersaturation exhaust pressure can vary from a hard vacuum to a rela- required in nuclei formation. The vapor pressure of tively high pressure and still produce colloidal particles. the propellent in the vaporizer 16 is controlled by regulat- The method and apparatus for generating colloidal io ing the power input to the heating unit 28. Particles according to the present invention can be used A predetermined supersaturation is required for nu- in numerous types of spacecraft. The colloidal particles cleation, and for some materials this state is reached =r /. 3,173,246 3 4 ahead of the nozzle throat. In this situation subsequent from metal foil that is supported on a relatively light expansion is not required for nucleation; however, the frame. expansion does cool these materials. This cooling is While one example of the invention has been dis- necessary to reject heat from the vapor stream to insuure closed and described it will be appreciated that various efficient formation of sub-micron colloidal particles from 5 modifications may be made to the structure as well as nuclei. The process is stopped with the formation of the method without departing from the spirit of the nuclei if low mass particles are desired. The formation invention or the scope of the subjoined claims. For ex- of the stable nuclei is quite complex and can vary from ample, it is contemplated that water as well as carbon 100 a.m.u.’s to over 600,000 a.m.u.3 for different ma- dioxide may be used as the propellent in the colloidal terials. 10 engine. While an important function of the nozzle 18 is to What is claimed is provide for supersaturation so that nuclei can be formed 1. A method of propulsion comprising the steps of from a given material, it further insures an adequate vaporizing a material, mass flow rate at a given supersaturation to provide a expanding said material in a supersonic node, con- sufficient quantity of nuclei suitable for use in an electro- 15 densing said material to form a plurality of sub- static engine. Also the length of the nozzle 18 is selected micron sized colloidal particles, to provide the required time necessary for nuclei forma- charging said particles, and tion and/or particle growth. The nozzle has an expan- accelerating said particles. sion ratio which not only provides the supersaturation 2. A method of propulsion comprising the steps of required for nuclei formation but also insures cooling so 20 heating a coloidal particle forming material to vapor- an efficient conversion of vapor to particles can occur ize the same, from a thermo-dynamlc viewpoint. expanding said vaporized material in a supersonic Particles in the range of 103 to 105 a.m.u.3 are pre- nozzle, ferred because they can be accelerated to a desired im- controlling the flow rate of said vaporized material in pulse by reasonable accelerating voltages.
Recommended publications
  • Chapter 3 Equations of State
    Chapter 3 Equations of State The simplest way to derive the Helmholtz function of a fluid is to directly integrate the equation of state with respect to volume (Sadus, 1992a, 1994). An equation of state can be applied to either vapour-liquid or supercritical phenomena without any conceptual difficulties. Therefore, in addition to liquid-liquid and vapour -liquid properties, it is also possible to determine transitions between these phenomena from the same inputs. All of the physical properties of the fluid except ideal gas are also simultaneously calculated. Many equations of state have been proposed in the literature with either an empirical, semi- empirical or theoretical basis. Comprehensive reviews can be found in the works of Martin (1979), Gubbins (1983), Anderko (1990), Sandler (1994), Economou and Donohue (1996), Wei and Sadus (2000) and Sengers et al. (2000). The van der Waals equation of state (1873) was the first equation to predict vapour-liquid coexistence. Later, the Redlich-Kwong equation of state (Redlich and Kwong, 1949) improved the accuracy of the van der Waals equation by proposing a temperature dependence for the attractive term. Soave (1972) and Peng and Robinson (1976) proposed additional modifications of the Redlich-Kwong equation to more accurately predict the vapour pressure, liquid density, and equilibria ratios. Guggenheim (1965) and Carnahan and Starling (1969) modified the repulsive term of van der Waals equation of state and obtained more accurate expressions for hard sphere systems. Christoforakos and Franck (1986) modified both the attractive and repulsive terms of van der Waals equation of state. Boublik (1981) extended the Carnahan-Starling hard sphere term to obtain an accurate equation for hard convex geometries.
    [Show full text]
  • Liquid-Vapor Equilibrium in a Binary System
    Liquid-Vapor Equilibria in Binary Systems1 Purpose The purpose of this experiment is to study a binary liquid-vapor equilibrium of chloroform and acetone. Measurements of liquid and vapor compositions will be made by refractometry. The data will be treated according to equilibrium thermodynamic considerations, which are developed in the theory section. Theory Consider a liquid-gas equilibrium involving more than one species. By definition, an ideal solution is one in which the vapor pressure of a particular component is proportional to the mole fraction of that component in the liquid phase over the entire range of mole fractions. Note that no distinction is made between solute and solvent. The proportionality constant is the vapor pressure of the pure material. Empirically it has been found that in very dilute solutions the vapor pressure of solvent (major component) is proportional to the mole fraction X of the solvent. The proportionality constant is the vapor pressure, po, of the pure solvent. This rule is called Raoult's law: o (1) psolvent = p solvent Xsolvent for Xsolvent = 1 For a truly ideal solution, this law should apply over the entire range of compositions. However, as Xsolvent decreases, a point will generally be reached where the vapor pressure no longer follows the ideal relationship. Similarly, if we consider the solute in an ideal solution, then Eq.(1) should be valid. Experimentally, it is generally found that for dilute real solutions the following relationship is obeyed: psolute=K Xsolute for Xsolute<< 1 (2) where K is a constant but not equal to the vapor pressure of pure solute.
    [Show full text]
  • Understanding Vapor Diffusion and Condensation
    uilding enclosure assemblies temperature is the temperature at which the moisture content, age, temperature, and serve a variety of functions RH of the air would be 100%. This is also other factors. Vapor resistance is commonly to deliver long-lasting sepa- the temperature at which condensation will expressed using the inverse term “vapor ration of the interior building begin to occur. permeance,” which is the relative ease of environment from the exteri- The direction of vapor diffusion flow vapor diffusion through a material. or, one of which is the control through an assembly is always from the Vapor-retarding materials are often Bof vapor diffusion. Resistance to vapor diffu- high vapor pressure side to the low vapor grouped into classes (Classes I, II, III) sion is part of the environmental separation; pressure side, which is often also from the depending on their vapor permeance values. however, vapor diffusion control is often warm side to the cold side, because warm Class I (<0.1 US perm) and Class II (0.1 to primarily provided to avoid potentially dam- air can hold more water than cold air (see 1.0 US perm) vapor retarder materials are aging moisture accumulation within build- Figure 2). Importantly, this means it is not considered impermeable to near-imperme- ing enclosure assemblies. While resistance always from the higher RH side to the lower able, respectively, and are known within to vapor diffusion in wall assemblies has RH side. the industry as “vapor barriers.” Some long been understood, ever-increasing ener- The direction of the vapor drive has materials that fall into this category include gy code requirements have led to increased important ramifications with respect to the polyethylene sheet, sheet metal, aluminum insulation levels, which in turn have altered placement of materials within an assembly, foil, some foam plastic insulations (depend- the way assemblies perform with respect to and what works in one climate may not work ing on thickness), and self-adhered (peel- vapor diffusion and condensation control.
    [Show full text]
  • Sub-Slab Vapor Sampling Procedures
    Sub-Slab Vapor Sampling Procedures RR-986 July 2014 Table of Contents I. Introduction .......................................................................................................................... 2 II. Sub-Slab Sample Ports .......................................................................................................... 2 A. Distribution of sub-slab probes ...................................................................................... 3 B. Permanent vs. temporary sub-slab probes .................................................................... 4 C. Tubing used in the sample train ..................................................................................... 4 D. Abandonment of sub-slab probes .................................................................................. 4 E. Sub-slab vapor samples collected from a sump pit ....................................................... 4 III. Leak Testing and Collecting a Sub-slab Sample .................................................................... 5 A. Shut-in test ..................................................................................................................... 6 B. Helium shroud ................................................................................................................ 7 C. Other leak detection methods for probe seals .............................................................. 7 D. Sample collection after leak testing ............................................................................... 8
    [Show full text]
  • Condensation Information October 2016
    Sun Windows General Information Section 1 Condensation Information October 2016 Condensation Every year, with the arrival of cold, winter weather, questions about condensation arise. The moisture that forms on window glass, obscuring the view, freezing or even collecting in puddles on the window sill, can be irritating and possibly even damaging. The first reaction may be to blame the windows for this problem, yet windows do not cause condensation. Excessive water vapor in the air, the temperature of the air and air circulation or movement are the three factors involved in the formation of condensation. Today’s modern homes are built very “air-tight” for energy efficiency. They provide better insulating properties and a cleaner, more comfortable living environment than older homes. These improvements in home design and construction have created some new problems as well. The more “air-tight” a home is the less fresh air that home circulates. A typical central air and heat system only circulates the air already within the home. This air becomes saturated with by-products of normal living. One of these is water vapor. Excessive water vapor in the home will most likely show up as condensation on windows. Condensation on your windows is a warning sign that the relative humidity (the measure of water vapor in the air) in your home is too high. You may see it develop on your windows, but it may be damaging the structural components and finishes through-out your home. It can also be damaging to your health. The following review should answer many questions concerning condensation and provide good information that will help in controlling condensation.
    [Show full text]
  • VAPOR-LIQUID EQUILIBRIA Using the Gibbs Energy and the Common Tangent Plane Criterion
    ChE curriculum VAPOR-LIQUID EQUILIBRIA Using the Gibbs Energy and the Common Tangent Plane Criterion MARÍA DEL MAR OLAYA, JUAN A. REYES-LABARTA, MARÍA DOLORES SERRANO, ANTONIO MARCILLA University of Alicante • Apdo. 99, Alicante 03080, Spain hase thermodynamics is often perceived as a difficult overall composition. This is the case with the binary system subject with which many students never become fully in Figure 1(a); it is homogeneous for all compositions. The gM comfortable. It is our opinion that the Gibbsian geo- vs. composition curve is concave down, meaning that no split Pmetrical framework, which can be easily represented in Excel occurs in the global mixture composition to give two liquid spreadsheets, can help students to gain a better understanding phases. Geometrically, this implies that it is impossible to find of phase equilibria using only elementary concepts of high two different points on the gM curve sharing a common tangent school geometry. line. In contrast, the change of curvature in the gM function Phase equilibrium calculations are essential to the simula- as shown in Figure 1(b) permits the existence of two conju- tion and optimization of chemical processes. The task with gated points (I and II) that do share a common tangent line these calculations is to accurately predict the correct number and which, in turn, lead to the formation of two equilibrium of phases at equilibrium present in the system and their com- liquid phases (LL). Any initial mixture, as for example zi in positions. Methods for these calculations can be divided into Figure 1(b), located between the inflection points s on the M 2 M dx2 two main categories: the equation-solving approach (K-value g curve, is intrinsically unstable (d g / i <0) and splits method) and minimization of the Gibbs free energy.
    [Show full text]
  • Redefining Volatile for Vocs
    South Coast Air Quality Management District 21865 Copley Drive, Diamond Bar, CA 91765-4182 (909) 396-2000 • http://www.aqmd.gov Non-Volatile, Semi-Volatile, or Volatile: Redefining Volatile for Volatile Organic Compounds Uyên-Uyên T. Võ, Michael P. Morris ABSTRACT The term volatile organic compound (VOC) is poorly defined because measuring volatility is subjective. There are numerous standardized tests designed to determine VOC content, each with an implied method to determine volatility. The parameters (time, temperature, reference material, column polarity, etc.) used in the definitions and the associated test methods were created without a significant evaluation of volatilization characteristics in real world settings. Not only do these differences lead to varying VOC content results, but occasionally they conflict with one another. An ambient evaporation study of selected analytes and a few formulated products was conducted and the results were compared to several current VOC test methodologies, as follows: SCAQMD Method 313 (M313), ASTM Standard Test Method E 1868-10 (E1868) and U.S. EPA Reference Method 24 (M24). The ambient evaporation study showed a definite distinction between non-volatile, semi-volatile and volatile compounds. Some low vapor pressure (LVP) solvents, currently considered exempt as a VOC by some methods, volatilize at ambient conditions nearly as rapidly as the traditional high volatility solvents they are meant to replace. Conversely, bio-based and heavy hydrocarbons did not readily volatilize, though they often are calculated as VOCs in some traditional test methods. The study suggests that regulatory standards should be reevaluated to better reflect these findings to more accurately reflect real world emission from the use of VOC containing products.
    [Show full text]
  • Phase Separation in Deionized Colloidal Systems: Extended Debye-Hu1 Ckel Theory
    Phase Separation in Deionized Colloidal Systems: Extended Debye-Hu1 ckel Theory Derek Y. C. Chan,*,† Per Linse,‡ and Simon N. Petris† Particulate Fluids Processing Centre, Department of Mathematics & Statistics, The University of Melbourne, Parkville VIC 3010, Australia, and Physical Chemistry 1, Center of Chemistry and Chemical Engineering, Lund University, P.O. Box 124, S-22100 Lund, Sweden Received November 8, 2000. In Final Form: May 3, 2001 Using an extension of the Debye-Hu¨ ckel theory for strong electrolytes, the thermodynamics, phase behavior, and effective pair colloidal potentials of deionized charged dispersions have been investigated. With the inclusion of colloid size effects, this model predicts the possibility of the existence of two critical points, one of which is thermodynamically metastable but can exhibit interesting behavior at high colloid charges. This analytic model also serves as a pedagogic demonstration that the phase transition is driven by cohesive Coulomb interactions between all charged species in the system and that this cohesion is not inconsistent with a repulsive effective pair potential between the colloidal particles. Introduction actions based on the Deryaguin-Landau-Verwey-Over- beek4 (DLVO) picture, the colloidal dispersion is treated In a series of very careful experimental studies, Ise et 1 as a one-component fluid of colloidal particles interacting al. demonstrated that stable deionized aqueous disper- under a combination of attractive dispersion forces and sions of polystyrene latex colloids exhibit simultaneously repulsive electrical double layer forces. In particular, the regions of high and low colloid densities. When the density electrical double layer interaction between identically of the latex particles is carefully matched with that of the charged particles is repulsive for all separations.
    [Show full text]
  • Vapor Intrusion Assessments Performed During Site Investigations Petroleum Remediation Program I
    www.pca.state.mn.us Vapor intrusion assessments performed during site investigations Petroleum Remediation Program I. Introduction This document describes the methodology for completing a vapor intrusion (VI) assessment at a site in the Minnesota Pollution Control Agency’s (MPCA) Petroleum Remediation Program (PRP). Vapor intrusion is the migration of volatile organic compounds (VOCs) from an underground source through soil or other pathways into buildings. A VI assessment is required when completing a site investigation within PRP. The goal of a VI assessment is to evaluate the VI pathway associated with a petroleum release. The VI pathway has three elements: receptor, vapor source, and subsurface migration route. A receptor is a person potentially affected by VI, generally an occupant of a building. A vapor source is the supply of VOCs, such as contaminated soil or groundwater or light non-aqueous phase liquids (LNAPL). A subsurface migration route is the path that vapors travel through soil or other pathways in the unsaturated zone. The VI assessment uses field-based methods to evaluate the VI pathway, including a receptor survey, soil gas sampling, sub-slab sampling, and indoor air sampling. For additional background information, see Technical Guide For Addressing Petroleum Vapor Intrusion At Leaking Underground Storage Tank Sites (EPA 2015) and Petroleum Vapor Intrusion Fundamentals of Screening, Investigation, and Management (ITRC 2014). II. Step 1 - Soil gas assessment Complete a soil gas assessment while defining the extent and magnitude of soil and groundwater impacts. There are limited situations in which the MPCA may preapprove a different scope of work than what is described here.
    [Show full text]
  • 3.3 Definitions & Notes PHASE CHANGES
    3.3 Definitions & Notes PHASE CHANGES WORDS FOR DEFINITIONS YOU NEED ARE IN RED Phase Heat of Heat of Endothermic exothermic change fusion vaporization vaporization Evaporation Vapor condensation sublimation pressure deposition PHASE CHANGE: thermal energy (HEAT) is transferred to or from a substance that causes a change in phase. During a phase change the temperature of the substance does not change A phase change is reversible ( can be undone or the substance can be returned to its original state) Phase change is a physical change, NOT A CHEMICAL CHANGE. Why doesn’t temperature change during a phase change? The thermal energy is consumed while breaking bonds. EXAMPLES: Ice absorbs heat to melt to liquid water. Liquid water gives off heat and freezes. TRANSITION: when a substance is moving from one phase to another it is in TRANSITION As a verb “ A substance is transitioning” – changing. EXO THERMIC: when heat is given off (Ex means – outside) ENDO THERMRIC: when heat is taken in THE TRANSITIONS WE ALREADY KNOW TRANSITION Description The transition from solid to liquid Melting Heat is absorbed by substance or added to substance The transition from liquid to solid Freezing Heat is given off by substance or absorbed by the surroundings The transition from Gas to liquid Condensation Heat is given off by substance or absorbed by the surroundings The transition from Liquid to Gas AT the Boiling point Vaporization Heat is absorbed by substance or added to substance The transition from Liquid to Gas BELOW the Boiling Evaporation point Heat is absorbed by substance or added to substance THE TRANSITIONS WE MAY NOT ALREADY KNOW TRANSITION Description The transition from solid directly to gas SUBLIMATION Heat is absorbed by substance or added to substance Example? The transition from gas directly to solid DEPOSITION Heat is given off by the substance or taken away Example? Data from Melting/Freezing Lab done with Napthalene TEMPERATURE CHANGING Do I need to write this down? Write down what you need.
    [Show full text]
  • Vapor and Gas Barriers Critical Building Protection
    PROVIDING A FULL BUILDING ENVELOPE SYSTEM VAPOR AND GAS BARRIERS CRITICAL BUILDING PROTECTION 13895-57277 Meadows-2021.indd 1 5/4/21 2:16 PM VAPOR RETARDANT STANDARDS The importance of a proven vapor and/or gas barrier. Uncontrolled water vapor through concrete slabs has cost building Underslab Vapor Barriers owners, designers and contractors billions of dollars. This moisture The use of underslab vapor barriers is the best method and infiltration into structures contributes to the proliferation of mold, most economical solution for controlling water vapor migration mildew and fungus that can lead to flooring system failures, through concrete slabs. The issue of admixtures and topically including adhesive failures, warping, blistering and staining. In applied materials does not address the issue that concrete cracks addition, water vapor migration carrying alkali can cause structural or the potential for elevated PH levels. failure of the concrete when reinforcing steel is present. ASTM E1993 and ASTM E1745 are the two industry standards Issues Directly Related to Flooring System Failures for vapor barriers and retarders under concrete slabs in contact • Many flooring systems used today form vapor barriers on top with soil. Note that typical polyethylene film does not meet the of concrete slabs and therefore trap water and alkali between requirements of these standards. the flooring system and the slab. Why Use a Gas Barrier? • 1999 federal mandate on VOC emissions created the need and In addition to the concern for moisture protection, other below- use of water-based flooring adhesives. grade contaminants have been identified as being major issues when it comes to occupant health and safety.
    [Show full text]
  • Condensation Fact Sheet
    Condensation Fact Sheet METAL BUILDING MANUFACTURERS ASSOCIATION The Condensation Process In metal building systems, we are concerned with two different Condensation occurs when warmer moist air comes in contact areas or locations: visible condensation which occurs on with cold surfaces such as framing members, windows and surfaces below dew point temperatures; and concealed other accessories, or the colder region within the insulation condensation which occurs when moisture has passed into envelope (if moisture has penetrated the vapor retarder). Warm interior regions and then condenses on a surface that is below air, having the ability to contain more moisture than cold air, the dew point temperature. loses that ability when it comes in contact with cool or cold surfaces or regions. When that happens, excessive moisture Signs of visible surface condensation are water, frost or ice on in the air is released in the form of condensation. In metal windows, doors, frames, ceilings, walls, floor, insulation vapor buildings, there are two possible consequences of trapped retarders, skylights, cold water pipes and/or cooling ducts. To moisture in wall and roof systems: (1) corrosion of metal effectively control visible condensation, it is necessary to reduce components and (2) degradation of the thermal performance of the cold surface areas where condensation may occur. It is also insulation. important to minimize the air moisture content within a building by the use of properly designed ventilating systems. Dew Point and Relative Humidity Dew point is the temperature at which water vapor in any Signs of concealed condensation include damp spots, stains, static or moving air column will condense into water.
    [Show full text]