CN106288417A - The double modulation of aqueous vapor rises the control method that gas heater leaving water temperature is preferential - Google Patents

The double modulation of aqueous vapor rises the control method that gas heater leaving water temperature is preferential Download PDF

Info

Publication number
CN106288417A
CN106288417A CN201610778858.XA CN201610778858A CN106288417A CN 106288417 A CN106288417 A CN 106288417A CN 201610778858 A CN201610778858 A CN 201610778858A CN 106288417 A CN106288417 A CN 106288417A
Authority
CN
China
Prior art keywords
temperature
actual
water
leaving water
gas heater
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.)
Granted
Application number
CN201610778858.XA
Other languages
Chinese (zh)
Other versions
CN106288417B (en
Inventor
易维宾
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.)
Foshan Hansen Electrical Appliance Industry Co., Ltd.
Original Assignee
易维宾
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 易维宾 filed Critical 易维宾
Priority to CN201610778858.XA priority Critical patent/CN106288417B/en
Publication of CN106288417A publication Critical patent/CN106288417A/en
Application granted granted Critical
Publication of CN106288417B publication Critical patent/CN106288417B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H9/00Details
    • F24H9/20Arrangement or mounting of control or safety devices
    • F24H9/2007Arrangement or mounting of control or safety devices for water heaters
    • F24H9/2035Arrangement or mounting of control or safety devices for water heaters using fluid fuel

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Control Of Combustion (AREA)
  • Control Of Temperature (AREA)

Abstract

The present invention relates to the double modulation of a kind of aqueous vapor and rise the control method that gas heater leaving water temperature is preferential, described gas heater includes fuel assembly, water outlet proportion valve, water flow sensing unit, inflow temperature sensor and the leaving water temperature sensors being connected with microcomputer control system, water flow sensing unit is for detecting the water yield of water outlet proportioning valve, inflow temperature sensor and leaving water temperature sensors are respectively used to detect inflow temperature and the leaving water temperature of water outlet proportioning valve, it is characterized in that: comprise the following steps: first, by formula TIf=Lmax*TGo out/LRealCalculate, then the actual water yield of adjusting water outlet proportioning valve and/or the real output of fuel assembly, make the actual leaving water temperature of gas heater preferentially equal to the design temperature of gas heater.

Description

The double modulation of aqueous vapor rises the control method that gas heater leaving water temperature is preferential
Technical field
The present invention relates to the double modulation of a kind of aqueous vapor and rise the control method that gas heater leaving water temperature is preferential.
Background technology
In prior art, gas heater be the maximum nominal value to set water outlet of water heater amount as benchmark, then use Family manually sets temperature required use, and during use, the instability of water temperature reduces the comfort of user, lacks people Property, and the occupation mode manually regulated is very inconvenient, and user is manually turning down water temperature, also can make because homoiothermic is inaccurate Become the waste of the energy.
Summary of the invention
It is an object of the invention to provide the double modulation of a kind of aqueous vapor and rise the control method that gas heater leaving water temperature is preferential, It is realized actual leaving water temperature be preferentially equal to design temperature, to improve users'comfort and easy to use by the most double tune of aqueous vapor Degree, to overcome weak point of the prior art.
The object of the present invention is achieved like this:
The double modulation of a kind of aqueous vapor rises the control method that gas heater leaving water temperature is preferential, and gas heater includes with micro computer controlled Fuel assembly, water outlet proportion valve, water flow sensing unit, inflow temperature sensor and leaving water temperature sensors, the water that system processed connects Flow sensor is for detecting the water yield of water outlet proportioning valve, and inflow temperature sensor and leaving water temperature sensors are respectively used to detection The inflow temperature of water outlet proportion valve and leaving water temperature, it comprises the following steps:
Microcomputer control system is defeated according to the actual water yield of below equation adjusting water outlet proportioning valve and/or the reality of fuel assembly Go out power, make the actual leaving water temperature of gas heater preferentially equal to the design temperature of gas heater:
TIf=Lmax*TGo out/LReal
TIfFor the design temperature of gas heater, LmaxFor the maximum output water yield of gas heater, TGo outMaximum for gas heater Leaving water temperature during the output water yield, LRealActual water yield after regulating for gas heater, Lmax*TGo out/LRealAdjust for gas heater After joint actual leaving water temperature, TGo outTemperature numerical by microcomputer control system according to inflow temperature and the reality of fuel assembly Output calculates and draws.
In described step, when design temperature is more than leaving water temperature, microcomputer control system preferentially increases fuel assembly Real output, so that actual leaving water temperature is preferentially equal to design temperature, if the real output of fuel assembly reaches Maximum, when design temperature is still more than actual leaving water temperature, microcomputer control system reduces the actual water outlet of water outlet proportion valve Amount, so that actual leaving water temperature is preferentially equal to design temperature.
In described step, when design temperature is equal to leaving water temperature, the reality of microcomputer control system detection fuel assembly Whether output has been maxed out value, when real output reaches maximum, keeps the reality of now water outlet proportion valve Water yield, so that actual leaving water temperature is preferentially equal to setting temperature, when real output is not reaching to maximum, micro computer controlled System processed continues whether the actual water yield of detection water outlet proportioning valve reaches maximum, if actual water yield reaches max water yield Time, keep actual water yield and the real output of fuel assembly of now water outlet proportion valve, so that actual leaving water temperature Preferential equal to design temperature, if actual water yield is not up to max water yield, increase the actual water outlet of water outlet proportion valve simultaneously Amount and fuel assembly real output until this two numerical value one of them reach when maximum or setting value be Only, so that actual leaving water temperature is preferentially equal to design temperature.
In described step, when design temperature is less than leaving water temperature, microcomputer control system preferentially increases water outlet proportion valve Actual water yield so that actual leaving water temperature is preferentially equal to design temperature, if the actual water yield of water outlet proportion valve reaches Maximum, when design temperature is still more than actual leaving water temperature, microcomputer control system reduces the actual output work of fuel assembly Rate, so that actual leaving water temperature is preferentially equal to design temperature.
Beneficial effects of the present invention is as follows:
The present invention in use, according to the contrast of design temperature Yu leaving water temperature, is automatically adjusted the reality of water outlet proportion valve Water yield and the real output of fuel assembly, it is achieved actual leaving water temperature preferentially equal to design temperature, it is ensured that actual go out Coolant-temperature gage is maintained at temperature constant state, thus increases substantially comfort and the degree easy to use that user uses, the most favourable In saving the energy.
Accompanying drawing explanation
Fig. 1 is the control principle drawing of one embodiment of the invention.
Detailed description of the invention
Below in conjunction with embodiment, the invention will be further described.
Seeing Fig. 1, the double modulation of this aqueous vapor rises the control method that gas heater leaving water temperature is preferential, described gas heater Including the fuel assembly being connected with microcomputer control system, water outlet proportion valve, water flow sensing unit, inflow temperature sensor and water outlet Temperature sensor, water flow sensing unit senses for detecting the water yield of water outlet proportioning valve, inflow temperature sensor and leaving water temperature Device is respectively used to detect inflow temperature and the leaving water temperature of water outlet proportioning valve, and it comprises the following steps:
Microcomputer control system is defeated according to the actual water yield of below equation adjusting water outlet proportioning valve and/or the reality of fuel assembly Go out power, make the actual leaving water temperature of gas heater preferentially equal to the design temperature of gas heater:
T sets=and Lmax*T goes out/and L is real;
T is set to the design temperature of gas heater, and Lmax is the maximum output water yield of gas heater, and T goes out for gas heater Leaving water temperature during the maximum output water yield, the actual water yield after the regulation of L actually gas heater, Lmax*T goes out/L actually combustion gas Water heater regulation after actual leaving water temperature, the Temperature numerical that T goes out by microcomputer control system according to inflow temperature and burning The real output of assembly calculates.
In above-mentioned steps, when design temperature is more than leaving water temperature, microcomputer control system preferentially increases fuel assembly Real output, so that actual leaving water temperature is preferentially equal to design temperature, if the real output of fuel assembly reaches Maximum, when design temperature is still more than actual leaving water temperature, microcomputer control system reduces the actual water outlet of water outlet proportion valve Amount, so that actual leaving water temperature is preferentially equal to design temperature.
Use sight one (as a example by the gas heater by complete machine maximum output water yield 16L):
Condition is set: design temperature: 65 DEG C;Set water yield: 10L.
Detect through microcomputer control system and obtain inflow temperature: 20 DEG C;Actual water yield: 10L;Leaving water temperature is: 45 DEG C. I.e. microcomputer control system is judged as that design temperature is more than leaving water temperature, and the real output of fuel assembly does not reaches maximum Value, the preferential real output increasing fuel assembly.
When the real output of fuel assembly reaches maximum, inflow temperature detected through microcomputer control system: 20 ℃;Actual water yield: 10L;Leaving water temperature is: 60 DEG C.I.e. microcomputer control system is judged as that design temperature is still more than water outlet Temperature, now, reduces the actual water yield of water outlet proportion valve, so that actual leaving water temperature is preferentially equal to design temperature.Finally Microcomputer control system detects inflow temperature: 20 DEG C;Actual water yield: 8.8L;Leaving water temperature is: 65 DEG C.
In above-mentioned steps, when design temperature is equal to leaving water temperature, the reality of microcomputer control system detection fuel assembly Whether output has been maxed out value, when real output reaches maximum, keeps the reality of now water outlet proportion valve Water yield, so that actual leaving water temperature is preferentially equal to setting temperature, when real output is not reaching to maximum, micro computer controlled System processed continues whether the actual water yield of detection water outlet proportioning valve reaches maximum, if actual water yield reaches max water yield Time, keep actual water yield and the real output of fuel assembly of now water outlet proportion valve, so that actual leaving water temperature Preferential equal to design temperature, if actual water yield is not up to max water yield, increase the actual water outlet of water outlet proportion valve simultaneously Amount and fuel assembly real output until this two numerical value one of them reach when maximum or setting value be Only, so that actual leaving water temperature is preferentially equal to design temperature.
Use sight two (as a example by the gas heater by complete machine maximum output water yield 16L):
Condition is set: design temperature: 45 DEG C;Set water yield: 10L.
Detect through microcomputer control system and obtain inflow temperature: 20 DEG C;Actual water yield: 8L;Leaving water temperature is: 45 DEG C. I.e. microcomputer control system is judged as that design temperature is equal to leaving water temperature, and actual water yield is less than setting water yield, now, Can increase actual water yield and the real output of fuel assembly of water outlet proportion valve simultaneously, thus keep actual go out water temperature Degree is preferential equal to design temperature, and meets the use requirement of water yield.Final microcomputer control system detects inflow temperature: 20 ℃;Actual water yield: 10L;Leaving water temperature is: 45 DEG C.
In above-mentioned steps, when design temperature is less than the step of leaving water temperature, microcomputer control system preferentially increases water outlet The actual water yield of proportioning valve, so that actual leaving water temperature is preferentially equal to design temperature, if the actual water outlet of water outlet proportion valve Amount reaches maximum, and when design temperature is still more than actual leaving water temperature, microcomputer control system reduces the reality of fuel assembly Output, so that actual leaving water temperature is preferentially equal to design temperature.
Use sight three (as a example by the gas heater by complete machine maximum output water yield 16L):
Condition is set: design temperature: 40 DEG C;Set water yield: 10L.
Detect through microcomputer control system and obtain inflow temperature: 30 DEG C;Actual water yield: 5L;Leaving water temperature is: 55 DEG C. I.e. microcomputer control system is judged as that design temperature is less than leaving water temperature, and the actual water yield of water outlet proportion valve is less than setting Water yield, now, the preferential actual water yield increasing water outlet proportion valve.
The actual water yield of water outlet proportion valve, equal to setting water yield, detects inflow temperature through microcomputer control system: 30℃;Actual water yield: 10L;Leaving water temperature is: 42.5 DEG C.I.e. microcomputer control system is judged as that design temperature is still less than Leaving water temperature, now, reduces the real output of fuel assembly, so that actual leaving water temperature is preferentially equal to design temperature. Final microcomputer control system detects inflow temperature: 30 DEG C;Actual water yield: 10L;Leaving water temperature is: 40 DEG C.
Use sight four (as a example by the gas heater by complete machine maximum output water yield 16L):
Condition is set: design temperature: 35 DEG C;Set water yield: 10L.
Detect through microcomputer control system and obtain inflow temperature: 30 DEG C;Actual water yield: 5L;Leaving water temperature is: 50 DEG C. I.e. microcomputer control system is judged as that design temperature is less than leaving water temperature, and the actual water yield of water outlet proportion valve is less than setting Water yield, now, the preferential actual water yield increasing water outlet proportion valve.
The actual water yield of water outlet proportion valve, equal to setting water yield, detects inflow temperature through microcomputer control system: 30℃;Actual water yield: 10L;Leaving water temperature is: 40 DEG C.I.e. microcomputer control system is judged as that design temperature is still less than out Coolant-temperature gage, now, reduces the real output of fuel assembly.
When the real output of fuel assembly is down to minimum, inflow temperature detected through microcomputer control system: 30 DEG C; Actual water yield: 10L;Leaving water temperature is: 38 DEG C.I.e. microcomputer control system is judged as that design temperature is still less than out water temperature Degree, now, will continue to increase the actual water yield of water outlet proportion valve.Final microcomputer control system detects inflow temperature: 30 ℃;Actual water yield: 16L;Leaving water temperature is: 35 DEG C.
By above-mentioned use sight, microcomputer control system by gas ratio valve, water proportioning valve are adjusted, Ensure, by the way of the double tune of aqueous vapor, the control that leaving water temperature is preferential, enable the invention to realize to promote user's comfort and Degree easy to use, and save the energy further.
The above-mentioned preferred version for the present invention, has been shown and described the ultimate principle of the present invention, principal character and the present invention Advantage.Those skilled in the art it should be recognized that the present invention is not restricted to the described embodiments, above-described embodiment and description Described in the principle that the present invention is simply described, the present invention also has various without departing from the spirit and scope of the present invention Changes and improvements, these changes and improvements both fall within scope of the claimed invention.Claimed scope is by institute Attached claims and equivalent thereof define.

Claims (4)

1. the double modulation of aqueous vapor rises the control method that gas heater leaving water temperature is preferential, and described gas heater includes with micro- Fuel assembly, water outlet proportion valve, water flow sensing unit, inflow temperature sensor and the leaving water temperature sensing that computerized control system connects Device, water flow sensing unit is for detecting the water yield of water outlet proportioning valve, and inflow temperature sensor and leaving water temperature sensors are used respectively Inflow temperature and leaving water temperature in detection water outlet proportioning valve, it is characterised in that: comprise the following steps:
Microcomputer control system is defeated according to the actual water yield of below equation adjusting water outlet proportioning valve and/or the reality of fuel assembly Go out power, make the actual leaving water temperature of gas heater preferentially equal to the design temperature of gas heater:
TIf=Lmax*TGo out/LReal
TIfFor the design temperature of gas heater, LmaxFor the maximum output water yield of gas heater, TGo outMaximum for gas heater Leaving water temperature during the output water yield, LRealActual water yield after regulating for gas heater, Lmax*TGo out/LRealAdjust for gas heater After joint actual leaving water temperature, TGo outTemperature numerical by microcomputer control system according to inflow temperature and the reality of fuel assembly Output calculates and draws.
The most according to claim 1, the double modulation of aqueous vapor rises the control method that gas heater leaving water temperature is preferential, and its feature exists In: in described step, when design temperature is more than leaving water temperature, the reality that microcomputer control system preferentially increases fuel assembly is defeated Go out power, so that actual leaving water temperature is preferentially equal to design temperature, if the real output of fuel assembly reaches maximum, When design temperature is still more than actual leaving water temperature, microcomputer control system reduces the actual water yield of water outlet proportion valve, thus Make actual leaving water temperature preferentially equal to design temperature.
The most according to claim 1, the double modulation of aqueous vapor rises the control method that gas heater leaving water temperature is preferential, and its feature exists In: in described step, when design temperature is equal to leaving water temperature, the actual output work of microcomputer control system detection fuel assembly Whether rate has been maxed out value, when real output reaches maximum, keeps the actual water yield of now water outlet proportion valve, So that actual leaving water temperature is preferentially equal to setting temperature, when real output is not reaching to maximum, microcomputer control system Whether the actual water yield continuing detection water outlet proportioning valve reaches maximum, if actual water yield reaches max water yield, protects Hold actual water yield and the real output of fuel assembly of now water outlet proportion valve, so that actual leaving water temperature priority scheduling In design temperature, if actual water yield is not up to max water yield, increase actual water yield and the combustion of water outlet proportion valve simultaneously Till when burning the real output of assembly one of them reach maximum or setting value until these two numerical value, thus Make actual leaving water temperature preferentially equal to design temperature.
The most according to claim 1, the double modulation of aqueous vapor rises the control method that gas heater leaving water temperature is preferential, and its feature exists In: in described step, when design temperature is less than leaving water temperature, microcomputer control system preferentially increases the reality of water outlet proportion valve Water yield, so that actual leaving water temperature is preferentially equal to design temperature, if the actual water yield of water outlet proportion valve reaches maximum, When design temperature is still more than actual leaving water temperature, microcomputer control system reduces the real output of fuel assembly, thus Make actual leaving water temperature preferentially equal to design temperature.
CN201610778858.XA 2016-08-31 2016-08-31 Water outlet temperature priority control method for water-gas double-modulation rising gas water heater Active CN106288417B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610778858.XA CN106288417B (en) 2016-08-31 2016-08-31 Water outlet temperature priority control method for water-gas double-modulation rising gas water heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610778858.XA CN106288417B (en) 2016-08-31 2016-08-31 Water outlet temperature priority control method for water-gas double-modulation rising gas water heater

Publications (2)

Publication Number Publication Date
CN106288417A true CN106288417A (en) 2017-01-04
CN106288417B CN106288417B (en) 2020-01-07

Family

ID=57672720

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610778858.XA Active CN106288417B (en) 2016-08-31 2016-08-31 Water outlet temperature priority control method for water-gas double-modulation rising gas water heater

Country Status (1)

Country Link
CN (1) CN106288417B (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108286788A (en) * 2017-01-10 2018-07-17 青岛经济技术开发区海尔热水器有限公司 The control method and gas heater of the variable gas heater of heat production outlet capacity
CN112484310A (en) * 2020-11-12 2021-03-12 华帝股份有限公司 Control method of electric water regulating valve of gas water heater
CN113433988A (en) * 2021-06-23 2021-09-24 深圳安吉尔饮水产业集团有限公司 Control method and device of heating system, heating system and storage medium
CN115111783A (en) * 2021-03-19 2022-09-27 保音股份有限公司 Power control method of water heater
CN115111784A (en) * 2022-06-24 2022-09-27 宁波方太厨具有限公司 Temperature control method and device for water heater, water heater and storage medium

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20080011245A1 (en) * 2006-07-12 2008-01-17 Emerson Electric Co. Control for a fuel-fired water heating appliance having variable heating rates
CN101109576A (en) * 2007-05-18 2008-01-23 海尔集团公司 Thermostatic control method for instantaneously heated water heater
CN102022832A (en) * 2009-09-11 2011-04-20 海尔集团公司 Water temperature control device and water temperature control method for gas water heater
CN103344046A (en) * 2013-06-28 2013-10-09 海尔集团公司 Constant-temperature gas heater control method and constant-temperature gas heater
CN104236109A (en) * 2013-06-24 2014-12-24 海尔集团公司 Control method and control device of constant-temperature gas water heater
CN104296386A (en) * 2013-07-18 2015-01-21 海尔集团公司 Control method and system of gas water heater and gas water heater
CN104676900A (en) * 2015-01-16 2015-06-03 芜湖美的厨卫电器制造有限公司 Gas water heater and control method thereof

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20080011245A1 (en) * 2006-07-12 2008-01-17 Emerson Electric Co. Control for a fuel-fired water heating appliance having variable heating rates
CN101109576A (en) * 2007-05-18 2008-01-23 海尔集团公司 Thermostatic control method for instantaneously heated water heater
CN102022832A (en) * 2009-09-11 2011-04-20 海尔集团公司 Water temperature control device and water temperature control method for gas water heater
CN104236109A (en) * 2013-06-24 2014-12-24 海尔集团公司 Control method and control device of constant-temperature gas water heater
CN103344046A (en) * 2013-06-28 2013-10-09 海尔集团公司 Constant-temperature gas heater control method and constant-temperature gas heater
CN104296386A (en) * 2013-07-18 2015-01-21 海尔集团公司 Control method and system of gas water heater and gas water heater
CN104676900A (en) * 2015-01-16 2015-06-03 芜湖美的厨卫电器制造有限公司 Gas water heater and control method thereof

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108286788A (en) * 2017-01-10 2018-07-17 青岛经济技术开发区海尔热水器有限公司 The control method and gas heater of the variable gas heater of heat production outlet capacity
CN112484310A (en) * 2020-11-12 2021-03-12 华帝股份有限公司 Control method of electric water regulating valve of gas water heater
CN112484310B (en) * 2020-11-12 2022-04-26 华帝股份有限公司 Control method of electric water regulating valve of gas water heater
CN115111783A (en) * 2021-03-19 2022-09-27 保音股份有限公司 Power control method of water heater
CN113433988A (en) * 2021-06-23 2021-09-24 深圳安吉尔饮水产业集团有限公司 Control method and device of heating system, heating system and storage medium
CN115111784A (en) * 2022-06-24 2022-09-27 宁波方太厨具有限公司 Temperature control method and device for water heater, water heater and storage medium

Also Published As

Publication number Publication date
CN106288417B (en) 2020-01-07

Similar Documents

Publication Publication Date Title
CN106288417A (en) The double modulation of aqueous vapor rises the control method that gas heater leaving water temperature is preferential
CN104236109B (en) The control method and control device of constant temp gas water heater
CN102022832B (en) Water temperature control device and water temperature control method for gas water heater
US8544761B2 (en) User activated hot water heater and control system
CN102278820B (en) Constant-temperature-type gas water heater control system with rapid and accurate temperature-regulating characteristic and control method
JP2015536016A5 (en)
CN106556151A (en) A kind of fuel gas of fuel gas water heater automatic pressure unit and method
CN107238207B (en) Control method of gas water heater and gas water heater
CN104807067B (en) The intelligent control method of combustion system and wind turbine in bathroom heating equipment
CN206771762U (en) One kind is according to the pressure controlled gas water heater control system of gas secondary
CN106403281B (en) Water heater control method, water heater controller and water heater
EP3312523A1 (en) Gas water heater and safety control system and method therefor
CN107655048B (en) Range hood and constant air quantity adjusting method and system thereof
WO2018040446A1 (en) Gas water heater and security control system and method therefor
CN108679852A (en) A kind of gas heater with gas flowmeter
TWI408318B (en) Water heater water temperature control method and device
CN205351793U (en) Constant temperature gas heater controller
US8381689B2 (en) Method for examining water heater safety
US20130071261A1 (en) Method of detecting safety of water heater
CN206001676U (en) Intelligent temperature controls gas heater
CN106284519A (en) A kind of constant temperature circulating water system
WO2018040447A1 (en) Gas water heater and security control system and method therefor
CN205747145U (en) A kind of high accuracy supply water temperature regulator control system
CN205245579U (en) Gas boiler's long -range temperature regulating device
CN105658934B (en) Control the method and gas-turbine plant of the emission of gas-turbine plant

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
TA01 Transfer of patent application right
TA01 Transfer of patent application right

Effective date of registration: 20191120

Address after: 528305 401, building 12, Zhifu garden, Shunde, No. 8, 2nd Ring Road, Gaozan village committee, Xingtan town, Shunde District, Foshan City, Guangdong Province

Applicant after: Foshan Hansen Electrical Appliance Industry Co., Ltd.

Address before: Fengkai Nanfeng County 526500 Guangdong city of Zhaoqing Province Jin Ming Cun Wei Hui Jinming No. 23

Applicant before: Yi Weibin

GR01 Patent grant
GR01 Patent grant