CN206256164U - A kind of depositing SiC equipment and its inlet duct - Google Patents

A kind of depositing SiC equipment and its inlet duct Download PDF

Info

Publication number
CN206256164U
CN206256164U CN201621396753.XU CN201621396753U CN206256164U CN 206256164 U CN206256164 U CN 206256164U CN 201621396753 U CN201621396753 U CN 201621396753U CN 206256164 U CN206256164 U CN 206256164U
Authority
CN
China
Prior art keywords
tank
exhaust outlet
inlet duct
mts
blending tank
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn - After Issue
Application number
CN201621396753.XU
Other languages
Chinese (zh)
Inventor
戴煜
胡祥龙
周岳兵
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Advanced Corp for Materials and Equipments Co Ltd
Original Assignee
Advanced Corp for Materials and Equipments Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Advanced Corp for Materials and Equipments Co Ltd filed Critical Advanced Corp for Materials and Equipments Co Ltd
Priority to CN201621396753.XU priority Critical patent/CN206256164U/en
Application granted granted Critical
Publication of CN206256164U publication Critical patent/CN206256164U/en
Withdrawn - After Issue legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The utility model provides a kind of inlet duct of depositing SiC equipment, including MTS fluid reservoirs, blending tank and surge tank, MTS fluid reservoirs are provided with hydrogen inlet manifold road, hydrogen inlet manifold road opening extend into MTS liquid levels lower section, fluid reservoir exhaust outlet is additionally provided with the top of MTS fluid reservoirs, fluid reservoir exhaust outlet is connected by the first pipeline with the first air inlet of blending tank, blending tank is additionally provided with the second air inlet, second air inlet is used to be input into argon gas, blending tank is provided with blending tank exhaust outlet, blending tank exhaust outlet is connected by second pipe with the air inlet of surge tank, surge tank is provided with surge tank exhaust outlet, surge tank exhaust outlet is connected by the 3rd pipeline with the body of heater of depositing SiC equipment.Inlet duct of the present utility model, sets blending tank and surge tank, and process gas is also easier to control by that can reduce pressure oscillation, the pressure of gas after two tank bodies.

Description

A kind of depositing SiC equipment and its inlet duct
Technical field
The utility model belongs to chemical vapor depsotition equipment field, and in particular to a kind of air inlet dress of depositing SiC equipment Put.
Background technology
Gas phase deposition technology is, using physics, the chemical process occurred in gas phase, functional gold to be formed in workpiece surface Category, nonmetallic or compound coat.Chemical vapor deposition refers to anti-containing the gaseous reactant or liquid for constituting film element Answer the steam of agent and other gases introduce reative cell needed for reaction, the process of chemical reaction generation film occurs in substrate surface.
Depositing SiC equipment is used for material surface ORC and matrix with trichloromethyl silane (MTS) as source of the gas It is modified.For the deposition effect for obtaining, it is necessary to which flow and pressure to MTS carry out accurate control, it is ensured that deposition gas in burner hearth Stream stabilization, pressure oscillation is within the scope of specifying.Existing depositing SiC equipment inlet duct, is existed using hydrogen and argon gas Mixed in MTS fluid reservoirs, then carry MTS gases and be directly entered body of heater, gas pulsation is larger, and cracked gas stream is unstable, Cause deposition velocity unstable, coating is uneven, the associativity of coating material is bad.
Utility model content
Technical problem to be solved in the utility model is, there is provided one kind can precise control depositing SiC equipment enter The inlet duct of atmospheric pressure.In order to solve the above-mentioned technical problem, the technical solution adopted in the utility model is:
A kind of inlet duct of depositing SiC equipment, including MTS fluid reservoirs, blending tank and surge tank, the MTS liquid storages Tank is provided with hydrogen inlet manifold road, and hydrogen inlet manifold road opening extend into MTS liquid levels lower section, the top of the MTS fluid reservoirs Portion is additionally provided with fluid reservoir exhaust outlet, and the fluid reservoir exhaust outlet passes through the first air inlet phase of the first pipeline and the blending tank Even, the blending tank is additionally provided with the second air inlet, and second air inlet is used to be input into argon gas, and the blending tank is provided with blending tank Exhaust outlet, the blending tank exhaust outlet is connected by second pipe with the air inlet of the surge tank, and the surge tank is provided with slow Tank exhaust outlet is rushed, the surge tank exhaust outlet is connected by the 3rd pipeline with the body of heater of depositing SiC equipment.
Further, in the utility model is a kind of preferred embodiment, the depositing SiC equipment in such scheme Inlet duct also include controller, pressure transmitter and electric control valve, the pressure transmitter be arranged on the surge tank or On 3rd pipeline, the electric control valve is arranged on the 3rd pipeline, the pressure transmitter and the controller It is connected, the controller is connected with the electric control valve, the controller receives pressure transmitter signal post-processing and exports Control signal gives the electric control valve.
Further, the pressure transmitter sensing unit described in such scheme is ceramic diaphragm.
It is further preferred that the admission pressure control accuracy in the 3rd pipeline is higher than ± Pa.
On the other hand, on the basis of above-mentioned inlet duct, the utility model additionally provides a kind of depositing SiC equipment, Including inlet duct and body of heater, the inlet duct is connected with the body of heater, wherein, the inlet duct is specially such scheme In any one inlet duct.
Inlet duct of the present utility model, there is provided blending tank and surge tank, hydrogen is introduced into MTS fluid reservoirs, then takes Band MTS gases are mixed into blending tank with argon gas, enter back into surge tank, are finally entered body of heater and are deposited.Mixing is set Tank and surge tank, process gas are also easier to control by that can reduce pressure oscillation, the pressure of gas after two tank bodies.
Brief description of the drawings
In order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art, below will be to embodiment Or the accompanying drawing to be used needed for description of the prior art is briefly described, it should be apparent that, drawings in the following description are only It is that, in order to more fully understand the utility model, and should not be construed to limitation of the present utility model.For the common skill in this area For art personnel, on the premise of not paying creative work, other accompanying drawings can also be obtained according to the accompanying drawing for providing.
Fig. 1 is a kind of structural representation of preferred embodiment of inlet duct of depositing SiC equipment described in the utility model Figure
Specific embodiment
In order that those skilled in the art more fully understand the technical scheme in the application, below in conjunction with the application reality The accompanying drawing in example is applied, the technical scheme in the embodiment of the present application is clearly and completely described, it is clear that described implementation Example is only some embodiments of the present application, rather than whole embodiments.
Refer to Fig. 1, the inlet duct of the depositing SiC equipment that the present embodiment is provided, including MTS fluid reservoirs 1, mixing Tank 2 and surge tank 3, MTS fluid reservoirs 1 are provided with hydrogen inlet manifold road 11, and the opening of hydrogen inlet manifold road 11 is extend under MTS liquid levels Side, the top of MTS fluid reservoirs 1 is additionally provided with fluid reservoir exhaust outlet 12, and fluid reservoir exhaust outlet 12 is by the first pipeline 51 and blending tank 2 The first air inlet 21 be connected, blending tank 2 is additionally provided with the second air inlet 22, and the second air inlet 22 is used to be input into argon gas, blending tank 2 The exhaust outlet of blending tank 2 is provided with, the exhaust outlet of blending tank 2 is connected by second pipe 52 with the air inlet 31 of surge tank 3, surge tank 3 Surge tank exhaust outlet 32 is provided with, surge tank exhaust outlet 32 is connected by the 3rd pipeline 53 with the body of heater 4 of depositing SiC equipment.
Depositing SiC equipment in technical process, for the deposition effect for obtaining, it is necessary to the flow and pressure of MTS Carry out accurate control, it is ensured that deposition steady air current in burner hearth, pressure oscillation is within the scope of specifying.If gas pulsation compared with Greatly, cracked gas stream is unstable, is easy for causing deposition velocity unstable, and coating is uneven, and the associativity of coating material is bad.This The inlet duct of embodiment, there is provided blending tank 2 and surge tank 3, hydrogen is introduced into MTS fluid reservoirs 1, then carries MTS gases Mixed with argon gas into blending tank 2, entered back into surge tank 3, finally entered body of heater 4 and deposited.Blending tank 2 is set to ease up Tank 3 is rushed, process gas is also easier to control by that can reduce pressure oscillation, the pressure of gas after two tank bodies.
The inlet duct of above-mentioned depositing SiC equipment can also be improved as follows:
Wherein, depositing SiC equipment inlet duct also includes controller, pressure transmitter 6 and electric control valve 7, pressure Transmitter 6 is arranged on the pipeline 53 of surge tank 3 or the 3rd, and electric control valve 7 is arranged on the 3rd pipeline 53, pressure transmitter 6 It is connected with controller, controller is connected with electric control valve 7, controller receives the signal post-processing of pressure transmitter 6 and exports control Signal processed is to electric control valve 7.The stream pressure signal that the detection of pressure transmitter 6 on 3rd pipeline 53 enters before body of heater 4, so After pass to controller, controller is processed signal according to process conditions, output control signal control electric control valve 7 enter Row regulation, can realize the recent pressure control accurate of body of heater 4.
Because MTS has strong corrosivity, the sensing unit of pressure transmitter 6 is ceramic diaphragm in such scheme, can Acid-resistant anti-corrosion, can under the acid atmosphere of MTS long-term use.
Preferably, the admission pressure control accuracy in the 3rd pipeline 53 is higher than ± 15Pa.
On the other hand, on the basis of above-mentioned inlet duct, the utility model additionally provides a kind of depositing SiC equipment, Including inlet duct and body of heater 4, inlet duct is connected with body of heater 4, wherein, inlet duct is specially any one in such scheme Plant inlet duct.
The above is only the specific embodiment of the application, it is noted that for the ordinary skill of the art For personnel, the improvement without creative work made on the premise of the application principle is not departed from all is considered as the application's Protection domain.

Claims (5)

1. a kind of inlet duct of depositing SiC equipment, it is characterised in that:Ease up including MTS fluid reservoirs (1), blending tank (2) Tank (3) is rushed, the MTS fluid reservoirs (1) are provided with hydrogen inlet manifold road (11), and hydrogen inlet manifold road (11) opening extend into MTS liquid levels lower section, is additionally provided with fluid reservoir exhaust outlet (12), the fluid reservoir exhaust outlet (12) at the top of the MTS fluid reservoirs (1) It is connected with first air inlet (21) of the blending tank (2) by the first pipeline (51), the blending tank (2) is additionally provided with second and enters Gas port (22), second air inlet (22) is for being input into argon gas, and the blending tank (2) is provided with blending tank (2) exhaust outlet, described Blending tank (2) exhaust outlet is connected by second pipe (52) with the air inlet (31) of the surge tank (3), the surge tank (3) Surge tank exhaust outlet (32) is provided with, the surge tank exhaust outlet (32) is by the 3rd pipeline (53) and the stove of depositing SiC equipment Body (4) is connected.
2. the inlet duct of depositing SiC equipment according to claim 1, it is characterised in that:Also include controller, pressure Power transmitter (6) and electric control valve (7), the pressure transmitter (6) are arranged on the surge tank (3) or the 3rd pipeline (53) on, the electric control valve (7) is arranged on the 3rd pipeline (53), the pressure transmitter (6) and the control Device is connected, and the controller is connected with the electric control valve (7), and the controller is located after receiving pressure transmitter (6) signal Manage and output control signal is to the electric control valve (7).
3. the inlet duct of depositing SiC equipment according to claim 2, it is characterised in that:Described pressure transmitter (6) sensing unit is ceramic diaphragm.
4. the inlet duct of the depositing SiC equipment according to claim 1-3 any one, it is characterised in that:Described Admission pressure control accuracy in three pipelines (53) is higher than ± 15Pa.
5. a kind of depositing SiC equipment, including inlet duct and body of heater (4), the inlet duct are connected with the body of heater (4), It is characterized in that:The inlet duct is specially the inlet duct described in claim 1-4 any one.
CN201621396753.XU 2016-12-19 2016-12-19 A kind of depositing SiC equipment and its inlet duct Withdrawn - After Issue CN206256164U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621396753.XU CN206256164U (en) 2016-12-19 2016-12-19 A kind of depositing SiC equipment and its inlet duct

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621396753.XU CN206256164U (en) 2016-12-19 2016-12-19 A kind of depositing SiC equipment and its inlet duct

Publications (1)

Publication Number Publication Date
CN206256164U true CN206256164U (en) 2017-06-16

Family

ID=59030377

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201621396753.XU Withdrawn - After Issue CN206256164U (en) 2016-12-19 2016-12-19 A kind of depositing SiC equipment and its inlet duct

Country Status (1)

Country Link
CN (1) CN206256164U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106435527A (en) * 2016-12-19 2017-02-22 湖南顶立科技有限公司 Silicon carbide deposition apparatus and air inlet device thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106435527A (en) * 2016-12-19 2017-02-22 湖南顶立科技有限公司 Silicon carbide deposition apparatus and air inlet device thereof
CN106435527B (en) * 2016-12-19 2019-02-05 湖南顶立科技有限公司 A kind of depositing SiC equipment and its inlet duct

Similar Documents

Publication Publication Date Title
CN106435527B (en) A kind of depositing SiC equipment and its inlet duct
CN105604653A (en) Urea jet control method and device and SCR system
CN206256164U (en) A kind of depositing SiC equipment and its inlet duct
CN207294886U (en) Tube furnace and chemical vapor deposition unit
CN208918809U (en) Air compressor performance test system
CN202974749U (en) Gas distributing device for simulating alcohol content of exhaled air by saturated vapor method
CN203363652U (en) Quantitative gas supply system
CN108395113A (en) Online float glass process coated glass transition roller table SO2Protect gas system and operating method
CN202756813U (en) Flow controller
CN205559107U (en) Natural -gas engine gas -supply system
CN208406660U (en) The air distributing device commonly combined with purifying
CN109680263A (en) A kind of precipitation equipment and a kind of atomic layer deposition apparatus
CN206751918U (en) A kind of device of thermal filament chemical vapor deposition of diamond film
CN110273141A (en) A kind of chemical vapour deposition reactor furnace for liquid precursor
CN103924216B (en) Plasma generator gas mixing pipe road
CN207483837U (en) Anti-soil film liquid plated film medicinal material automatic medicine adding apparatus
CN210856329U (en) Chemical vapor deposition system and gas supply device
CN105331925B (en) A kind of high-precision dynamic vacuum control system for vacuum nitriding
CN208406664U (en) Multimode gas-liquid mixed control system
CN207713813U (en) A kind of novel reaction in chemical vapor deposition equipment controls spray equipment
CN103028339B (en) Gas-water mixing device and gas-water combined supply system
CN207493482U (en) It is a kind of to supply ammonia system heating unit
CN207091471U (en) Novel evacuated heat treatment bleeder mechanism
CN106048559B (en) A kind of nano particle apparatus for atomic layer deposition and method based on space isolation
CN209493630U (en) The source MO center fed system

Legal Events

Date Code Title Description
GR01 Patent grant
AV01 Patent right actively abandoned
AV01 Patent right actively abandoned

Granted publication date: 20170616

Effective date of abandoning: 20190205