You guys have got the right Idea just the wrong application, I dont know if it will make much difference, but what I am trying to do is control the humidity in an oven for cooking hams, bacon and sauages, for this process to work correctly for commerical cooking it is paramount that we keep the humidity at a set point, so that we do not loose too much moisture out of the product.
The thing that I dont understand with using the wet and dry bulb calculation is the pressure, we dont have any way of measuring pressure in the oven, so because of this and the fact that we are not introducing pressure, and we are acting at atmospheric pressure, I suppose that we can insert a value of one for the pressure (I am not sure)?
Being that this is an oven, I might want to change my answer. I'm not sure of what easily available psychrometric data/charts exist for such high temperatures.
If your data are based on atmospheric pressure, that would be zero rather than one.
If based on absolute pressure, full vacuum equals zero, and atmospheric equals 14.68 psi, subject to altitude correction.
I'll try to look around for some high-temperature data; no promise of success, though.
As a practical matter, you could add a shallow pan of water to the oven, replenishing it as necessary. Now if we can just pin down the instrumentation.... And even then, you may need to do your own experimentation.
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In vino veritas; in cervisia carmen; in aqua E. coli.
Hmmm, I'd say that your given application is a vital and missing note in your original post. In normal applications where humidity is concerned saturated air has a relative humidity of 100%. This of course does not apply to the generation of steam, which will be generated in an oven at cooking temperatures greater than 100C. At the temperatures experienced in an oven you will generate steam, which then is a whole different set of conditions where "humidity" does not apply.
BTW, Psychrometric charts do not apply beyond 100C (the boiling point of water).
I suggest you analyze your humidity control issue from a whole-system perspective first starting with the equipment and working forward to your final product requirements and specifications. Though by no means an expert, having invested the last 25 years almost exclusively in the food processing equipment and meat production industries (with all aspects of freezers, chillers, blanchers, ovens and smokehouses) I consider myself sufficiently experienced to offer recommendations and suggestions. I am presently working on two separate large smoke-house oven projects for processing cured hams and pork-bellies.
If I correctly assume your equipment is commercial or light-industrial (in terms of equipment operation, performance and mechanical design) then I put forward there are numerous, measurable, substantial and frequently changing pressure-zones inside your smoke house(s) during any typical cycle. Consequently, measuring and/or controlling humidity merits a thorough and comprehensive analysis of all relevant aspects of the entire process as well as all products to be smoked.
Issues to fully understand and consider - specific to humidity control include: 1.) Product i.e. weight, size, age of animals, temperature, etc. 2.) Brine i.e. pre-cook characteristics of products, brine percentage, salinity, other important constituents, temperature, injection methods, drip-loss etc. 3.) Smokehouse i.e. style, type, specific fan performance, air velocities, air exchanges, cook cycles etc; 4.) Smoke generation i.e. natural, wood-fired, liquid smoke other; 5.) Process i.e. manual or automatic cook; cook temperature; recipe; post-cook product cooling; cooling time; further processing and packaging etc. 6.) Customer requirements and specifications – especially important to consider are all variants and even future product specifications and/or new customer specifications.
I've found that properly measuring and recording actual humidity levels inside a modern-day size operating smoke-house is challenging at best but not impossible. Accurately controlling humidity levels, through all phases of a typical smoke cycle, is achievable with the correct equipment and, most importantly consistent production operations.
I suspect we may be direct competitors in this industry. As one quick and relatively simple starting point, I recommend you consider contacting one of several manufacturers of industrial smoke-house ovens (such as Alkar RapidPak; Marlen; Powis Controls, or a host of smaller local manufacturers) as a starting point. I have worked with many competent sales-applications engineers who have always been willing to help further my knowledge and understanding of smokehouse ovens and specifically humidity controls.
With most smoke ovens that i have seen they only use the wet and dry bulb sensors, to calculate humidity. The wet one sits directly above a small vessel of water which has a soaked (water) cloth protruding from the water vessel and hung over the wet sensor.
The Dry sensor, does 2 jobs it measures the cabinet temperature (oven temp) and also is used as a reference for measuring the the temperature difference between the wet and dry bulbs.
We also know that if the values of the wet and dry bulb sensors are equal we have 100% humidity.
But the tricky part is because we are heating the oven at different temperatures and this temperature is varying all the time, we cannot use a simple calculation.
What we need to do is: depending on the cabinet temperature the cabinet can hold different amounts of humidified water ie; at a lower temperature the cabinet requires less water humidifed to acheive 100% humidity, but as the temperature rise's we will need more water humidifed to achieve 100% humidity.
I know that there is a formula that uses, these factors 1. cabinet temp 2. temp diff (Dry - Wet) with these values we then go to a reference chart and get a number.
But I cant remember where I came across this chart and I cant remember exactly how the calculation works.
The calculation is not required to be 100% accurate, +- 2% would be very accetable.
Also I dont think that it is necessarry to know which product you are cooking, in relation to the humidity as we are only controlling the humidity in the cabinet. The operator will select what humidity % he requires for the product he is cooking, depending on the weight loss that is accetable for that product, After all he may be doing products that require little or no humidity, so therefore it is up to the operator and his experience and his required result as to what the humidity should be.
As you have said Pork Man these is a bit of science and operator experience, that goes into cooking the product right, all operators have different idea's and different results.
Brilliant reply...thanks for clearing up this mystery in the low-temperature application of humidity and how it applies to "cooking" in an "oven". Thumbs up!
Iam a marine engineer & can explain only certain things in my
perspective.for measuring pressure inside oven u can use a pressure
difference method.how much less or more than atmospheric pressure,
using a u tube.
I am not sure where you are going with your posting, I dont want to measure pressure, I want to measure humidity. I am just having troubles working out calculations using a very basic anologurtherm for the calculation of the humidity, problem is I cant find a data table that is workable.
Or track these quantities on a psychrometric chart. (That's psychro-, not psycho-; I have never seen a psychometric chart, though it might be amusing....)
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Hi MrCarlos, the best one I found was the Vaisala site, the calculator is simple to use, but for my application if I wanted to calculate to the nearest degree, I would have to do about 9000 calculations and fit them in a data reference table, but that seems like to much work and use of data tables that I wanted to use for other applications in the software.
What I am trying to find is a simple calculation that uses the temperature (dry Bulb) and Dew Point (wet Bulb) and a simple look up table to calculate to finish the calculation.
I am sure that there is a calculation out there that goes somthing like this;
D - W = Tb
D x Tb = H%
Where:
D = Temperature
W = Dew Point Temp (Wet Bulb)
Tb = Look Up Table
H = Humidity %
I am not sure it my calcus is correct, I just have a feeling that I am working along the right lines.
Many Thanks to all that have are contributing to this forum.
It is really easy, you could find a lot off information about it on Meteorology area try with the Psichrometer procedure.
Here is something in spanish but sure there are information in english to.
· Psicrometro
Mide el contenido de humedad del aire.
Consta de dos termómetros idénticos de mercurio. A uno de ellos se le recubre el bulbo con una gasa que se humedece con agua destilada, se le llama termómetro húmedo. El otro termómetro mide la temperatura del aire, se llamatermómetro seco. El bulbo húmedo mide una temperatura igual o menor al bulbo seco, debido a que el agua que se evapora de la gasa, absorbe calor. La diferencia entre ambas medidas está relacionada, para cada temperatura y presión atmosférica, con el contenido de vapor de agua de la atmósfera.
Cuando la humedad relativa es de 100%, la lectura de ambos termómetros es igual. Cuando hay poca humedad en el aire, la gasa evapora más rápido y se nota más diferencia entre los dos termómetros.
see Perry, "The Chemical Engineer's Handbook", any edition, or
any HVAC textbook.
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RH is defined as the ratio of the mass of water vapour in a certain volume of moist air at a given temperature to the mass of water vapour in the same volume of saturated air at the same temperature. It is considered to be a more commonly understood measure of the degree of saturation of air. Psychrometer is used to measure R.H. It consists of dry and wet bulb thermometers fixed side by side on a wooden or metal plate. A dirty wick should be replaced from the wet bulb thermometer regularly. Before taking the readings the instrument should be whirled round rapidly for about a minute. R.H charts are available in the market. Once we know the DBT and WBT R.H cab be found from the chart.
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