This invention relates generally to a method of accurately measuring real-time dew-point value and total moisture content of a material. More specifically, it relates to accurately measuring the real-time valid dew-point value and estimating the total moisture content of the material within the valid dew-point value using an algorithm during a material drying process.
Currently, the existing material drying processes adopt various mechanisms to determine the real-time dew-point value of a material and to estimate the total moisture content of the material. However, these processes do not provide an accurate real-time dew-point estimate as the dew-point of the material may vary over a period during the material drying process. Further, the existing drying process does not allow the system to provide a valid dew-point value within which the system must be capable of estimating the total moisture content of the material.
The existing drying processes do not allow a system to provide a valid dew-point value within which the system must be capable of estimating the total moisture content of the material. Hence, there is a need for a system that provides an accurate real-time valid dew-point value within which the moisture content of the material can be determined during the material drying process.
PCT publication WO2013093942 discloses a method and a device for moisture determination and control using real-time measurement of the material moisture content at an inlet and outlet of the drying process, such as in a drying hopper. Here, the drying process is controlled by anticipating the drying load based on the moisture content of the incoming material to be dried.
CN 103399486 discloses a temperature optical energy-saving control method for a plastic dryer. The method adopts a predictive control strategy based on multi-model switching to identify dynamic characteristics of air temperature of the plastic dryer and establish a switching system model of an object under each typical working condition. An optical target function with constraint is established by utilizing a switching rule and a mixed neural network is formed by neural networks for processing a continuous variable and a discrete binary variable together.
U.S. Pat. No. 8,433,443 B2 relates to a method for on line monitoring of polymerization reaction in a fluid bed reactor to generate data indicative of imminent occurrence of a discontinuity event (such as sheeting). The method further relates to optional control of the reaction to prevent the occurrence of the discontinuity event.
CN 201672991 relates to a dry and wet bulb temperature acquisition device performing functions of dry and wet bulb temperature acquisition, wireless data receiving and transmitting, and dry and wet bulb temperature display.
U.S. Pat. No. 8,021,462 B2 relates to a dehumidification plant for granular materials having varying physicochemical characteristics, with energy consumption less than that of the dehumidification process, and to a process for regenerating at least one process tower in a granular material dehumidification plant.
EP 2186613 B1 relates to a high efficiency system for dehumidifying and/or drying plastic material. The system enables electronic process control of hopper parameters monitored through sensors and devices.
U.S. Pat. No. 6,289,606 B2 relates to an apparatus and a method for controlling moisture content of a particulate material in a hopper. The apparatus comprises a dew-point sensor to output a signal based on the sensed moisture content of the material and a control circuitry to cause the selector to operate based on output signal.
This invention provides a system and method for accurately measuring the real-time dew-point value of a material based on which the total moisture content of the material is determined. The method comprises of acquiring data from temperature sensors and dew-point sensors that are positioned at dryer outlets while performing the material drying process. The method receives the sensed data at a server from the sensors by using any of the existing data transmitting technologies such as programmable logic controller, a relay, or a wireless sensor network. Further, the method estimates the initial moisture content of the material before the drying process begins and estimates the total moisture content of the material at any instance during the drying process. The method measures a valid dew-point of the material by determining an inflection point of the moisture content as a function of time curve for the material and determines the total moisture content of the material based on that determined inflection point for the moisture versus time curve/function for the material. The material is preferably granular plastic resin; however the method is not limited to the granular plastic resin but has applicability to other materials that require drying or accurate determination of moisture content.
Other objects and advantages of the embodiments herein will become readily apparent from the following detailed description taken in conjunction with the accompanying drawings.
In the following detailed description, reference is made to the accompanying drawings that form a part hereof, and specific embodiments that may be practiced are shown by way of illustration. The embodiments are described in sufficient detail to enable those skilled in the art to practice the embodiments and it is to be understood that the logical, mechanical and other changes may be made without departing from the scope of the embodiments. The following detailed description is not to be taken in a limiting sense.
In accordance with the invention, the method uses an algorithm for accurately measuring the real-time valid dew-point value of a material. Total moisture content of the material is estimated within the determined valid dew-point value during the material drying process. The material used for the drying process can be a resin, a plastic, or the like.
A valid dew-point value 105 for the material inside the dryer unit 101 is determined by using an algorithm. An inflection point of the material moisture level as a function of time curve is determined for the material. Total moisture content of the material is determined based on the inflection point of the moisture as a function of time curve as estimated for the material by using the algorithm. The real-time valid dew-point value of the material is determined and is transmitted to hopper 102 for determining total moisture content of the material within the valid dew-point value by using the algorithm which provides the determination of the inflection point of the moisture content versus time curve for the material of interest.
U(t)=k∫0tDP({acute over (t)})*DAir({acute over (t)})*F({acute over (t)})d{acute over (t)} [1]
where DP({acute over (t)}) is the dew-point at a given time {acute over (t)} in the outlet, DAir({acute over (t)}) is the density of air (since outlet air temperature is changing) and F({acute over (t)}) is the flow rate, which remains constant all the time. A linear correction factor of k is assumed because dew-point measurement is never accurate and is used to offset the inaccurate dew-point.
Then, water vapor extracted from the material between any two given times t and t2, is given by
ΔU(t−t2)=k∫t2tDP({acute over (t)})*DAir({acute over (t)})*F({acute over (t)})d{acute over (t)} [2]
To determine the moisture content of the material as V(t), following mass conservation equation is applied, denoting total mass of material as Mp,
Mp*{V(t)−V(t2)}=ΔU(t−t2)=k∫t2tDP({acute over (t)})*DAir({acute over (t)})*F({acute over (t)})d{acute over (t)} [3]
Assuming t2=0th time or any other time from several sets of measurement of drying, k is determined from linear regression, which should remain constant as it reflects dew-point calibration adjustment.
Knowing k, the total amount of water in the material can be determined.
In one practice of the invention, the following algorithm is used to determine the initial moisture content of the material of interest:
Since within 15-30 minutes of the outlet air attaining highest and saturated temperature, material moisture content is expected to reduce to 50-100 parts per million (ppm), the following modification of equation [4] is used to approximate the residual moisture content, (assuming Td is the time to arrive at high-saturated temperature at outlet of the dryer):
Moisture vapor content of material at top at any given time during material cycling is determined using equation 6:
A control module 204 to transmits data across modules in system 200 using any existing data transmitting technology such as a programmable logic controller, a relay, a wireless sensor network and the like.
The method transmits the estimated valid dew-point value to hopper 102 within which the total moisture content of the material can be determined by the algorithm. For example, the curve for one material depicts a dew-point of 2000 ppm and the curve for the other material depicts a dew-point of 770 ppm, which have decreased over a period of time during the material drying process. The algorithm determines the total moisture content of the material within the valid dew-point value estimated for the material.
The foregoing description of the specific embodiments fully reveals the embodiments that others can, by applying current knowledge, readily modify and/or adapt these embodiments for various applications without departing from the generic concept. Therefore, such adaptations and modifications should and are intended to be comprehended within the meaning and range of equivalents of the disclosed embodiments. It is to be understood that the phraseology or terminology employed herein is for the purpose of description and not of limitation. Therefore, while the embodiments herein have been described in terms of preferred embodiments, those skilled in the art will recognize that the embodiments herein can be practiced with modification within the spirit and scope of the appended claims. Although the embodiments herein are described with various specific embodiments, a person skilled in the art will practice the invention with modifications. However, all such modifications are deemed to be within the scope of the claims.
This patent application is a 35 USC 120 division of pending U.S. patent application Ser. No. 15/049,098, entitled “Method for Accurately Measuring Real-Time Dew Point Value and Total Moisture Content of a Material”, filed 21 Feb. 2016 and published as United States patent publication 2016/0245765 A1 on 25 Aug. 2016. This application claims the priority of the '098 application under 35 USC 120. The '098 application claimed the priority of U.S. Provisional Patent application Ser. No. 62/119,293 filed Feb. 23, 2015, entitled “Method for Accurately Measuring Real-Time Dew-Point Value and Total Moisture Content of a Material”. This patent application claims the benefit of the priority of the '293 application through the '098 application; the priority is claimed under 35 USC 120.
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20190391096 A1 | Dec 2019 | US |
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Parent | 15049098 | Feb 2016 | US |
Child | 16562500 | US |