Title of Invention

A METHOD AND APPARATUS FOR CONTROLLING AN ATMOSPHERE IN A HEAT TREATMENT FURNACE

Abstract

In a method of and apparatus for controlling an atmosphere in a bent treatment funnace according to the present invention, a carburizing is carried out while supplying a hydrocarbon series gas and an oxidization gas into the furnace, and the supply of the hydrocarbon series gas is stopped either when the quantity of a residial CH4 in the furnace 5 changed to increasing from decreasing, or when a partial pressure of oxygen in the furnace reaches a predetermined value.

Full Text

- 14- CONTROL METHOD OF AND APPARATUS FOR ATMOSPHERE IN HEAT TREATMENT FURNACE BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to a method of and apparatus for controlling an atmosphere in a heat treatment furnace, and more particularly relates to a control method of and apparatus for an atmosphere in a heat treatment furnace for carrying out a gas carburizing, carbonitriding or bright controlled atmosphere heat treatment, etc. 2. Description of the Prior Art In the conventional heat treatment methods, such as a gas carburizing of metals, a mixture of a hydrocarbon series gas with air is generated into a converted gas (endothermic gas) by using an endothermic type converted gas generator, the endothermic gas is introduced into a furnace, and a hydrocarbon series gas (enriched gas) is added to the furnace in order to obtain a predetermined carbon potential. However, recently, in order to enhance the quality, and to reduce the treatment time and - 2 - running cost, such a method that the gas generator is not used, but a hydrocarbon series gas and an oxidizing gas are introduced directly into the furnace to carry out the carburizing in the furnace has been proposed. Such method is described in Japanese Patent Applications Laid-Open Nos. 54931/1979, 159567/1986 and 63260/1992. However, the carburizing speed in the direct carburizing method is varied on a large scale according to the carburizing time and the diffusion time- In the carburizing time, the main deficf teffect is the direct decomposition of the hydrocarbon series gas, etc. (raw gas.) and in difect the diffusion time, the main effect is the Boundouard reaction. In the carburizing time, the degree of the decomposition is different due to the quantity of the hydrocarbon series gas to be introduced directly into the furnace and the temperature of the atmosphere in the furnace as well as the type of goods to be treated in the furnace. As a result, the hydrocarbon series gas in excess of the amount required to the carburizing is piled as a soot in the furnace or the goods -3- to be treated are sooted. If the heat treatment is carried out in the sooting range, the service life of the oxygen sensor becomes short. SUMMARY OF THE INVENTION An object of the present invention is to obviate the above defects. Further object of the present invention is to provide a method of controlling an atmosphere in a heat treatment furnace comprising the steps of carrying out a carburizing while supplying a hydrocarbon series gas and an oxidization gas into a furnace, and stopping the supply of the hydrocarbon series gas when the quantity of a residual CH4 in the furnace is changed to increasing from decreasing. Another object of the present invention is to provide a method of controlling an atmosphere in a heat treatment furnace comprising the steps of carrying out a carburizing while supplying a hydrocarbon series gas and an oxidization gas into a furnace, and stopping the supply of the hydrocarbon series gas when the partial, pressure of oxygen in the furnace reaches a predetermined value. - 4 - Further object of the present invention is to provide a control apparatus for controlling an atmosphere in a furnace comprising a furnace, a heater for heating the inside of the furnace, means for measuring a partial pressure of oxygen and a partial pressure of CH4 in the furnace, means for introducing a hydrocarbon series gas and an oxidization gas into the furnace, and means for controlling the quantities of the hydrocarbon series gas and the oxidization gas to be introduced into the furnace. In the present invention, a liquid containing carbon atoms such as alcohol, gas such as acetylene, methane, propane or butane containing hydrocarbon for its main ingredient, preferably, methane, propane or butane is used as the hydrocarbon series gas. In the present invention, the oxidization gas is air or CO2 gas. The forgoing and other objects, features, and advantages of the present invention will become apparent from the following more particular description of preferred embodiments of the invention, as illustrated in the - 5 - accompanying drawings. "ACCOMPANYING" BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a view illustrating a control method and apparatus of an atmosphere in a heat treatment furnace in accordance with the present invention. Fig. 2 is a graph explaining the relationship between the effective case depth and the carburizing time according to the carbon potential. Fig. 3 is a graph explaining the relationship between the quantity of residual CH4 and the carburizing time according to the quantity of added enriched gas. Fig. 4 is a graph explaining the relationship between the quantity of undecomposed residual CH4 and the quantity of added C4M10 according to the carburizing time. DESCRIPTION OF THE PREFERRED EMBODIMENTS Fig. 1 shows a control apparatus for a heat treatment furnace according to the present invention. In Fig. 1, reference numeral 1 denotes a shell of furnace, 2 denotes a refractory brick forming the shell of furnace 1, 3 denotes a - 6 - fan for recirculating the atmosphere in the furnace, 4 denotes a heater, 5 denotes a thermocouple for controlling the temperature in the furnace, 6 denotes a zirconian type sensor for sensing the partial pressure of a solid electrolyte oxygen, for example, which is inserted directly into the furnace, 8 denotes a tube for measuring the partial pressure of CH4, 10 denotes an analyzer for analyzing the partial pressure of CH4, 11 denotes a pipe for introducing hydrocarbon series gas into the furnace, 12 denotes a control valve inserted into the pipe 11, 13 denotes a pipe for introducing oxidization gas into the furnace, 14 denotes a control valve inserted into the pipe 13, 15 denotes an operating apparatus for the carbon potential, and 16 denotes a controller for supplying control signals to the valves 12 and 14. Fig. 2, shows the relationship between the effective case depth and the carburizing time according to the carbon potential. As shown in Fig. 2, it is publicly known that if the carbon potential in the carburizing time is higher, the carburizing can be completed with a shorter time period and that it is not - 7 - suitable to carry out the heat treatment in the hatched sooting region of the Fe-C series equilibrium diagram shown in Fig. 2. It is better to add a large quantity of enriched gas (hydrocarbon series gas) in order to increase the carbon potential. As shown in Fig. 3, in each of cases that if the goods to be treated is 150kg and C4H20 gas of 2.5 liter/minute is introduced (case A), C4H10 gas of 1.4 liter/minute is introduced (case B), and C4H10 gas of 1.0 liter/minute is introduced (case C), the quantity of residual CH4 is decreased and then increased with time, so that the goods are sooted. However, in case that C4H10 gas of 0.5 liter/minute is introduced (case D), the quantity of residual CH4 is constant substantially, so that the goods are not sooted. It is considered that in the cases of (A), (B)and (C), the quantity of added C4H10 gas is large and accordingly some carbon cannot be absorbed by the steel, so that the quantity of undecomposed residual CH4 is increased, but in case of (D), entire carbon can be absorbed by the steel. Accordingly, the sooting can be prevented from occurring by - 8 - analyzing the quantity of residual CH4 and controlling it. In the present invention, therefore, the quantity of residual CH4 is analyzed by the analyzer 10 and when the quantity of residual CH4 is changed to increasing from decreasing the control valve 12 is closed to stop the supply of the hydrocarbon series gas CM Hy, so that the quantity of residual CH4 is prevented from being increased. As apparent from the Fe-C series equilibrium diagram, the sooting can be prevented from occurring by measuring the partial pressure of oxygen corresponding to the maximum carbon solid solution, because the maximum carbon solid solution is constant at a specific temperature. In the present invention, accordingly, the output value of the sensor 6 for sensing the partial pressure of oxygen is measured to know the partial pressure of oxygen, and the control valve 12 is closed when the partial pressure of oxygen reaches a predetermined value, in order to prevent the sooting from occurring. Further, in the present invention, the control valve 12 can be closed at an earlier -9- time either when the partial pressure of oxygen reaches a predetermined value or the partial pressure of CH4 reaches a predetermined value by carrying out the measurements of the partial pressure of oxygen and the measurement of the partial pressure of CH4 at the same time. (Embodiment 1) A batch furnace is used, the goods to be treated of 150kg are introduced into the furnace, and the carburizing operation is carried out for four hours at 9300C by using C4H10 gas as a hydrocarbon series gas and CO2 gas as an oxidization gas. As shown in Fig. 3, the quantity of CH4 increases with time in case that more than 1.0 liter/minute of butane is added as the hydrocarbon series gas. This means that the residual CH4 is undecomposed and accumulated in the furnace, so that the sooting is accelerated. Fig. 4 shows the relationship between the quantity of residual CH4 in the furnace and the quantity of added C4H10 according to the carburizing time, in case that no sooting is occurred. It is apparent from Fig. 4 that the sooting is occurred when the quantity of added - 10 - hydrocarbon series gas is 2.5 liter/minute, but the sooting can be prevented from occurring if the introduction of the hydrocarbon series gas is stopped according to the present invention. As the hydrocarbon series gas, a liquid containing carbon atoms, such as alcohol, or gas such as acetylene, methane, propane or butane gas containing a hydrocarbon for its main ingredient, preferably methane, propane or butane gas is used. Air or CO2 gas is used as the oxidization gas. As stated above,according to the present invention, the sooting can be prevented from occurring in advance by controlling the quantity of hydrocarbon series gas to be added according to the partial pressure of CH4 and partial pressure of oxygen in the atmosphere of the heat treatment for the gas carburizing, carbonitriding or bright heat treatment. While the invention has been particularly shown and described with reference to the preferred embodiments thereof, it will be understood by those skilled in the art that various changes in form and details may be made therein without departing from the spirit and - 11 - scope of the invention as defined by the appended claims. -12-WE CLAIM 1. A method of controlling an atmosphere in a heat treatment furnace comprising the steps of carrying out a carburizing while supplying a hydrocarbon series gas and an oxidization gas such as herein described, into a furnace, and stopping the supply of the hydrocarbon series gas when the quantity of a residual CH4 in the furnace is changed to increasing from decreasing. 2. A method of controlling an atmosphere in a heat treatment furnace comprising the steps of carrying out a carburizing while supplying a hydrocarbon series gas and an oxidization gas such as herein described, into a furnace, and stopping the supply of the hydrocarbon series gas when the partial pressure of oxygen in the furnace reaches a predetermined value. 3. The method of controlling an atmosphere in a heat treatment furnace as claimed in claim 1 or 2, further comprising the steps of stopping the supply of the hydrocarbon series gas of an earlier time either when the residual cH4 is -13- changed to increasing from decreasing or the partial pressure of oxygen in the furnace reaches a predetermined value. 4- The method of controlling an atmospher in a heat treatment furnace as claimed in claim 1, 2 or 3, wherein a liquid containing carbon ataos such 33 alcohol, gas such as acetylene, methane, propane or butane containing hydrocarbon for its main ingredient, preferably, methane, propane or butane is used as the hydrocarbon series east- 5. The method of controlling an atmosphere in a heat treatment- furnace as claimed in claim 1, 2, 3 or 4, wherein the oxidation gas is air or CO2 gas. 6. A control apparatus for controlling an atmosphere in a furnace comprising a furnace (1), a heater (4) for heating the inside of the furnace (1), means (6,8) for measuring a partial pressure of oxygen and a partial pressure of CH4 in the furnace (1), means (11,13) for introducing a hydrocarbon series gas and an oxidation gas into the furnace (1), and means (12,14) for controlling the quantities of the hydrocarbon series gas and the oxidation gas to be introduced into the furnace (1), said means to control the quantities of the hydrocarbon series gas and the oxidation gas comprising means to stop the supply of hydrocarbon series gas and/or oxidation gas when the quantity of residual CH4 changes to increasing from decreasing or the partial pressure of oxidation gas reaches a predetermined value. - 14 - 7. The control apparatus for controlling an atmosphere in a furnace as claimed in claim 6, wherein a liquid containing carbon atoms such as alcohol, gas such as acetylene, methane, propane or butane containing hydrocarbon for its main ingredient, preferably, methane, propane or butane is used as the hydrocarbon series gas. 8. The control apparatus for controlling an atmosphere in a furnace as claimed in claim 6 or 1, wherein the oxidization gas is air or CO2 gas. DATED THIS 11th DAY OF FEBRUARY 1998 In a method of and apparatus for controlling an atmosphere in a bent treatment funnace according to the present invention, a carburizing is carried out while supplying a hydrocarbon series gas and an oxidization gas into the furnace, and the supply of the hydrocarbon series gas is stopped either when the quantity of a residial CH4 in the furnace 5 changed to increasing from decreasing, or when a partial pressure of oxygen in the furnace reaches a predetermined value.

Documents:

00222-cal-1998-abstract.pdf

00222-cal-1998-claims.pdf

00222-cal-1998-correspondence.pdf

00222-cal-1998-description (complete).pdf

00222-cal-1998-drawings.pdf

00222-cal-1998-form-1.pdf

00222-cal-1998-form-2.pdf

00222-cal-1998-form-3.pdf

00222-cal-1998-form-5.pdf

00222-cal-1998-pa.pdf

00222-cal-1998-priority document others.pdf

00222-cal-1998-priority document.pdf

222-CAL-1998-FORM-27.pdf

222-cal-1998-granted-abstract.pdf

222-cal-1998-granted-acceptance publication.pdf

222-cal-1998-granted-claims.pdf

222-cal-1998-granted-correspondence.pdf

222-cal-1998-granted-description (complete).pdf

222-cal-1998-granted-drawings.pdf

222-cal-1998-granted-examination report.pdf

222-cal-1998-granted-form 1.pdf

222-cal-1998-granted-form 2.pdf

222-cal-1998-granted-form 3.pdf

222-cal-1998-granted-letter patent.pdf

222-cal-1998-granted-pa.pdf

222-cal-1998-granted-priority document.pdf

222-cal-1998-granted-reply to examination report.pdf

222-cal-1998-granted-specification.pdf

222-cal-1998-granted-translated copy of priority document.pdf