CN107417577A - The method and device of biuret is removed in urea for vehicle - Google Patents

The method and device of biuret is removed in urea for vehicle Download PDF

Info

Publication number
CN107417577A
CN107417577A CN201610346678.4A CN201610346678A CN107417577A CN 107417577 A CN107417577 A CN 107417577A CN 201610346678 A CN201610346678 A CN 201610346678A CN 107417577 A CN107417577 A CN 107417577A
Authority
CN
China
Prior art keywords
urea
filter
biuret
exchange resin
container
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.)
Pending
Application number
CN201610346678.4A
Other languages
Chinese (zh)
Inventor
胡坚南
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.)
Shandong Sealan Environmental Technology Co Ltd
Original Assignee
Shandong Sealan Environmental Technology 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 Shandong Sealan Environmental Technology Co Ltd filed Critical Shandong Sealan Environmental Technology Co Ltd
Priority to CN201610346678.4A priority Critical patent/CN107417577A/en
Publication of CN107417577A publication Critical patent/CN107417577A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C273/00Preparation of urea or its derivatives, i.e. compounds containing any of the groups, the nitrogen atoms not being part of nitro or nitroso groups
    • C07C273/02Preparation of urea or its derivatives, i.e. compounds containing any of the groups, the nitrogen atoms not being part of nitro or nitroso groups of urea, its salts, complexes or addition compounds
    • C07C273/14Separation; Purification; Stabilisation; Use of additives
    • C07C273/16Separation; Purification

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Treatment Of Liquids With Adsorbents In General (AREA)

Abstract

The invention discloses the method and device that biuret is removed in a kind of urea for vehicle, belong to the preparing technical field of urea for vehicle, methods described comprises the following steps:Weight of urea percentage is prepared as 31.8% 33.2% urea liquid;Obtained urea liquid cools to there is gonorrhoea state;The urea liquid filtering of gonorrhoea state is will appear from, until urea liquid is clarified;The mass percent for obtaining biuret is less than 0.3% urea for vehicle solution.Described device includes accommodating the container of urea liquid, the inside of the container is provided with agitating device, the container is sequentially communicated first filter and the second filter by pipeline, pipeline between the container and the first filter is provided with the first delivery pump, and the pipeline between the container and second filter is provided with the second delivery pump.Compared to the prior art, the present invention has method simple, removes the advantages of biuret effect is good.

Description

The method and device of biuret is removed in urea for vehicle
Technical field
The present invention relates to the preparing technical field of urea for vehicle, biuret is removed in specifically a kind of urea for vehicle Method and device.
Urea water plays the role of that Nox can be purified, and is widely used in the gas-purification system of large-scale diesel vehicle.Automobile Urea, it be a kind of use in SCR technology, for reducing the liquid of the nitrogen oxides pollution in exhaust gas from diesel vehicle.Automobile-used urine Plain scientific name is diesel engine vent gas treatment fluid, and the country is commonly called as automobile urea, urea for vehicle, automobile environment-protection urea, automobile-used denitrfying agent, made With it is most common be urea for vehicle.Urea for vehicle is used for reduction of nitrogen oxide, can be used as SCR (Selective Catalytic Reduction, SCR) system reducing agent, utilize the bavin such as the urea for vehicle aqueous solution and heavy truck, car Reaction of nitrogen oxides generation N in oily tail gas2And H2O carrys out cleaning of off-gas, its nitrogen oxides discharged is reached Europe IV discharges Standard.
Urea is in granulation process, and when temperature is more than 133 DEG C, condensation reaction will occur for urea, produces biuret, urine Plain water easily remains biuret in preparation process;Biuret can not separate out under normal temperature condition.Meanwhile the purity of urea for vehicle will Very high, common urea or urine is asked to can not meet requirement of the urea for vehicle to high-purity, the urea for vehicle product of in the market The problem of biuret that quality is extremely difficult in international standard, particularly urea for vehicle is exceeded, how to reduce in urea for vehicle and contract The content of two ureas turns into a serious problems for restricting urea for vehicle industry development.
At present, the method for reducing Biuret Content in urea product typically used is for recrystallization method and in evaporation process The formation of biuret is prevented, however, recrystallization method yield is low, cost is high;The effect of the formation of biuret is prevented in evaporation process Fruit is extremely limited.The method that also can reduce the content of biuret in urea for vehicle in positive exploration in the industry, such as such as Lower patent:
Chinese patent(CN 104289106 A)Disclose a kind of preparation method of urea for vehicle solution, its use it is not concentrated, Ammonia and CO be granulated and that remnants are removed through flash distillation2Afterwards, high-temperature high concentration urea solution is raw material, is used directly to produce automobile-used urine Plain solution.The method provided in the patent limits the finished product urea for vehicle produced by using the raw material of low Biuret Content In Biuret Content, although this method step is relatively simple, the production cost of its raw material is very high, the urea raw material into This is the several times of common urea, causes the production cost of urea for vehicle very high.
Chinese patent(CN 104402769 A)A kind of production technology of urea for vehicle is disclosed, by production technology Adjust to reduce the content of biuret in urea for vehicle product, still, the method for the patent operates sufficiently complex, required equipment Also it is more complicated, cause operability and production efficiency ratio relatively low.
In addition, the above method reduces biuret in urea for vehicle by changing the preparation technology of overall urea for vehicle Content, not individually remove urea for vehicle in biuret method.
The content of the invention
In view of the above-mentioned problems, it is an object of the invention to provide the method and dress that biuret is removed in a kind of urea for vehicle Put, this method strong operability and removal effect is good, common urea can be used to be substantially reduced automobile-used as raw material production urea for vehicle The production cost of urea;The apparatus structure is simple, for removing the biuret in urea for vehicle.
The present invention, which solves the technical scheme that its technical problem is taken, to be included:The method that biuret is removed in urea for vehicle, Comprise the following steps:
Step 1):Prepare the urea liquid that weight of urea percentage is 32.5%-65%;
Step 2):By step 1)In obtained urea liquid cool to there is gonorrhoea state;
Step 3):By step 2)The middle urea liquid filtering for gonorrhoea state occur, until urea liquid is clarified;
Step 4):The mass percent for obtaining biuret is less than 0.3% urea for vehicle solution.
Further technical scheme is:The step 1)Concrete operation method be urea to be put into deionized water, to going Ionized water is heated and is stirred simultaneously, until urea is completely dissolved, forms urea liquid.
To reach the best precipitation effect of biuret, further technical scheme is:The step 2)In, by urea liquid Cool to -5~17 DEG C.
For the filter effect reached, further technical scheme is:The step 3)In, urea liquid passes through two successively Level filtering, the filtering accuracy of first order filtering is 25 μm, and the filtering accuracy of second level filtering is 1 μm;Urine is kept in filter process The temperature of plain solution is constant, that is, keeps urea liquid in low-temperature condition.
Further technical scheme is:The first order filters and second level filtering uses ion exchange resin filter core.
From the point of view of filter effect, preferable technical scheme is:The ion exchange resin filter core is handed over for anion Change resin filter element.
Consider from economy and filter effect comprehensive angle, selectable technical scheme is:The ion exchange resin filter The filter core that core is anion exchange resin and cationic ion-exchange resin combination is formed, the wherein amount of anion exchange resin are more than sun The amount of ion exchange resin.
Further technical scheme is:The urea liquid flows through first order filtering and flows through the flow velocity of second level filtering not Together.Generally, the flow velocity that liquid stream filters through the first order is more than the flow velocity for flowing through second level filtering, filters step by step with maximum limit The biuret removed in urea liquid of degree.
The scheme that the present invention solves its technical problem also includes:The device of the above method is realized, including accommodates urea liquid Container, the inside of the container is provided with agitating device, and the container is sequentially communicated first filter and the second mistake by pipeline Filter, the pipeline between the container and the first filter are provided with the first delivery pump, the first filter with it is described Pipeline between second filter is provided with the second delivery pump;It is temporary that solution is provided between the first filter and the second delivery pump Pond is deposited, the first filter and the second delivery pump are connected with the solution scratch pool.
Solution scratch pool is set, passes through the second delivery pump, thus it is possible to vary into the flow velocity of the solution of the second filter, is realized The flow velocity of double-filtration is different.
For ease of heating and cooling to solution, further technical scheme is:The bottom of the container is provided with heater, The side wall of the container is provided with cooling tube.
The beneficial effects of the invention are as follows:
1st, by the research of solubility and the relation of temperature to biuret, it is found that biuret solubility in low temperature can become Change, so as to realize the biuret removed by way of filtering in urea liquid, can substantially reduce in urea for vehicle product The content of biuret, method is simple, removal effect is good, solve tradition remove biuret recrystallization method yield is low, cost is high The problem of, so as to which realization produces urea for vehicle solution by the use of common urea as raw material, substantially reduce the production cost of urea for vehicle;
2nd, research is found, biuret separates out from urea liquid under low-temperature condition, makes urea liquid that gonorrhoea state be presented, precipitation Biuret ion is powered, therefore, using ion exchange resin as filter core, substantially increases filter effect and the effect filtered Rate.
3rd, the present apparatus is used to remove the biuret in urea liquid, and stirring and filtering are integrated in be formed on a device and flowed Ability of swimming operation, simple in construction, easy to operate, production efficiency is high.
4th, in device of the invention, contain and heater and cooler device is carried in the container of solution, be easy to solution in container Temperature be controlled, further improve operating efficiency;Dress centers liquid scratch pool, passes through the second delivery pump, thus it is possible to vary Into the flow velocity of the solution of the second filter, realize that the flow velocity of double-filtration is different, improve filter effect.
Brief description of the drawings
Fig. 1 is the structural representation of device of the embodiment of the present invention;
Fig. 2 is the curve map of biuret solubility and temperature relation.
In figure:1 solution tank, 2 stirring vanes, 3 heating tubes, 4 first delivery pumps, 5 first filters, 6 second delivery pumps, 7 Second filter, 8 solution scratch pools.
Embodiment
With reference to Figure of description and specific embodiment, the invention will be further described:
Embodiment one:
The method that biuret is removed in urea for vehicle, it comprises the following steps:
Step 1):Solid urea particle and purified water are inserted in solution tank, stirs to being completely dissolved, weight of urea percentage is made Than the urea liquid for 32.5%;
Step 2):Step 1)The process of middle solid urea particle dissolving is exothermic process, and obtained urea liquid is in low temperature shape State, by step 1)In obtained urea solution temperature be down to -5 DEG C, now gonorrhoea state is presented in urea liquid;
Step 3):Will appear from the urea liquid of gonorrhoea, to pass sequentially through filtering accuracy by pipeline pump be 25 μ first filters and mistake Filter precision is 1 the second filters of μ;
First filter inner filter core is anion exchange resin;Second filter element is that weight ratio is 8:2 anion exchange Resin and cationic ion-exchange resin;
The flow that urea liquid passes through first filter is 25L/min;The flow that urea liquid passes through the second filter is 15L/ min.During urea liquid is by first filter and the second filter, the temperature of urea liquid maintains -10 all the time ℃。
Step 4):Obtain the urea liquid of Biuret Content 0.25%.
Embodiment two:
The method that biuret is removed in urea for vehicle, it comprises the following steps:
Step 1):Solid urea particle and purified water are inserted in solution tank, to solid urea particle and the mixture of purified water Heated, the urea liquid for being completely dissolved, being made that weight of urea percentage is 45% is stirred while heating;
Step 2):By step 1)In obtained urea solution temperature be down to 0 DEG C, now gonorrhoea state is presented in urea liquid;
Step 3):Will appear from the urea liquid of gonorrhoea, to pass sequentially through filtering accuracy by pipeline pump be 25 μ first filters and mistake Filter precision is 1 the second filters of μ;
First filter inner filter core is that weight ratio is 9:1 anion exchange resin and cationic ion-exchange resin;Second filter Filter core is that weight ratio is 7:3 anion exchange resin and cationic ion-exchange resin;
The flow that urea liquid passes through first filter is 25L/min;The flow that urea liquid passes through the second filter is 15L/ min.During urea liquid is by first filter and the second filter, the temperature of urea liquid maintains 0 DEG C all the time.
Step 4):Obtain the urea liquid of Biuret Content 0.27%.
Embodiment three:
The method that biuret is removed in urea for vehicle, it comprises the following steps:
Step 1):Solid urea particle and purified water are inserted in solution tank, stirs to being completely dissolved, weight of urea percentage is made Than the urea liquid for 60%;
Step 2):Step 1)The process of middle solid urea particle dissolving is exothermic process, and obtained urea liquid is in low temperature shape State, by step 1)In obtained urea solution temperature be down to 8 DEG C, now gonorrhoea state is presented in urea liquid;
Step 3):Will appear from the urea liquid of gonorrhoea, to pass sequentially through filtering accuracy by pipeline pump be 25 μ first filters and mistake Filter precision is 1 the second filters of μ;
First filter inner filter core is that weight ratio is 9:1 anion exchange resin and cationic ion-exchange resin;Second filter Filter core is anion exchange resin;
The flow that urea liquid passes through first filter is 20L/min;The flow that urea liquid passes through the second filter is 12L/ min.During urea liquid is by first filter and the second filter, the temperature of urea liquid maintains -5 all the time ℃。
Step 4)Obtain the urea liquid of Biuret Content 0.24%.
The relation of solubility and temperature of the biuret in water is as shown in Fig. 2 with the reduction of temperature, the dissolving of biuret Degree drastically declines, and when temperature is below 17 DEG C, biuret almost separates out and maintains plateau completely, from cost consideration ,- 5~17 DEG C of temperature range is the most suitable, but when temperature is lower, has no effect on precipitation and filter effect, therefore, may be alternatively provided as Lower temperature.
In the method for the present invention, the series of filtering is not limited to double-filtration, can increase the series of filtering, by continuously carrying The pure amount for further reducing biuret, increase the transparency of solution, lift the quality of solution.In addition, improve the dense of urea liquid Degree can make adsorption effect more preferably.
As shown in figure 1, realizing the device of the above method, including the solution tank 1 of urea liquid is accommodated, the solution tank 1 Bottom is provided with stirring vane 2, and the solution tank 1 is sequentially communicated the filter 7 of first filter 5 and second by pipeline, described molten Pipeline between liquid bucket 1 and the first filter 5 is provided with the first delivery pump 4, the solution tank 1 and second filter Pipeline between 7 is provided with the second delivery pump 6.
Solution scratch pool 8, the first filter 5 and second are provided between the delivery pump 6 of first filter 5 and second Delivery pump 6 is connected with the solution scratch pool 8.Solution scratch pool 8 is set, passes through the second delivery pump 6, thus it is possible to vary is entered The flow velocity of the solution of second filter 7, realize that the flow velocity of double-filtration is different.Generally, the first filtering should be allowed fluid flow through The flow velocity of device 5 is more than the flow velocity for flowing through the second filter 7, sets multistage filtering to remove the contracting in urea liquid to greatest extent Two ureas.
Heating tube 3 is provided with the bottom of solution tank 1, the side wall of the solution tank 1 is provided with cooling tube(Not shown in figure). In order to realize the heating and cooling of solution in solution tank 1, heating tube 3 carries out heating to solution can accelerate solid urea particle Dissolution velocity, cooling tube can quickly cool, and urea liquid is quickly down to required temperature, improve operating efficiency.Molten Temperature sensor can be set in liquid bucket 1, using the detection signal of temperature sensor as signal source, to realize heating tube 3 and cooling tube The operating circuit of automatic work, heating tube 3 and cooling tube can be switched over by switching relay, or be entered by magnetic valve Row circuit is connected or disconnected, and automaticity is high, and the accuracy of control is improved while saving manpower.Relay switching electricity Road is the conventional control circuit of this area, and magnetic valve is also common component, to those skilled in the art, completely can root The setting to said elements is completed according to prior art, its specific method to set up will not be repeated here.
In the present invention, filter is not limited to set the two-stage described in embodiment, can increase the quantity of filter, Continuous purification is realized, in order to ensure filter effect, filter should at least set two-stage.
In the present invention, the ratio of anion exchange resin and cationic ion-exchange resin in filter is not limited to embodiment Disclosed in ratio, both ratios can be made a change because anion exchange resin to biuret ion absorption effect Fruit is more preferable, and to ensure filter effect, the amount of anion exchange resin should be greater than the amount of cationic ion-exchange resin, or all use Anion exchange resin.
The foregoing is merely illustrative of the preferred embodiments of the present invention, is not the whole embodiments of the present invention, not limiting The system present invention, within the spirit and principles of the invention, any modification, equivalent substitution and improvements made etc., should be included in Within protection scope of the present invention.
In addition to technical characteristic described in specification, remaining technical characteristic is technology known to those skilled in the art, in order to prominent Go out the innovative characteristicses of the present invention, above-mentioned technical characteristic will not be repeated here.

Claims (10)

1. the method for biuret is removed in urea for vehicle, it is characterized in that, comprise the following steps:
Step 1):Prepare the urea liquid that weight of urea percentage is 32.5%-65%;
Step 2):By step 1)In obtained urea liquid cool to there is gonorrhoea state;
Step 3):By step 2)The middle urea liquid filtering for gonorrhoea state occur, until urea liquid is clarified;
Step 4):The mass percent for obtaining biuret is less than 0.3% urea for vehicle solution.
2. the method for biuret is removed in urea for vehicle according to claim 1, it is characterized in that, the step 1)It is specific Operating method is that urea is put into deionized water, and deionized water is heated and is stirred simultaneously, until urea is completely molten Solution, form urea liquid.
3. the method for biuret is removed in urea for vehicle according to claim 1, it is characterized in that, the step 2)In, will Urea liquid cools to -5~17 DEG C.
4. the method for biuret is removed in urea for vehicle according to claim 1, it is characterized in that, the step 3)In, urine Plain solution passes through double-filtration successively, and the filtering accuracy of first order filtering is 25 μm, and the filtering accuracy of second level filtering is 1 μm; Keep the urea solution temperature constant in filter process.
5. the method for biuret is removed in urea for vehicle according to claim 4, it is characterized in that, first order filtering and second Level filtering uses ion exchange resin filter core.
6. the method for biuret is removed in urea for vehicle according to claim 5, it is characterized in that, the ion exchange resin Filter core is anion exchange resin filter core.
7. the method for biuret is removed in urea for vehicle according to claim 5, it is characterized in that, the ion exchange resin The filter core that filter core is anion exchange resin and cationic ion-exchange resin combination is formed, the amount of wherein anion exchange resin are more than The amount of cationic ion-exchange resin.
8. the method for biuret is removed in urea for vehicle according to claim 4, it is characterized in that, the urea liquid flows through First order filtering is different with the flow velocity for flowing through second level filtering.
9. the device of the method described in claim 1 is realized, it is characterized in that, including accommodate the container of urea liquid, the container Inside be provided with agitating device, the container is sequentially communicated first filter and the second filter by pipeline, the container with Pipeline between the first filter is provided with the first delivery pump, between the first filter and second filter Pipeline is provided with the second delivery pump;Solution scratch pool, first mistake are provided between the first filter and the second delivery pump Filter and the second delivery pump are connected with the solution scratch pool.
10. device according to claim 9, it is characterized in that, the bottom of the container is provided with heater, the container Side wall is provided with cooling tube.
CN201610346678.4A 2016-05-24 2016-05-24 The method and device of biuret is removed in urea for vehicle Pending CN107417577A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610346678.4A CN107417577A (en) 2016-05-24 2016-05-24 The method and device of biuret is removed in urea for vehicle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610346678.4A CN107417577A (en) 2016-05-24 2016-05-24 The method and device of biuret is removed in urea for vehicle

Publications (1)

Publication Number Publication Date
CN107417577A true CN107417577A (en) 2017-12-01

Family

ID=60422542

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610346678.4A Pending CN107417577A (en) 2016-05-24 2016-05-24 The method and device of biuret is removed in urea for vehicle

Country Status (1)

Country Link
CN (1) CN107417577A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108715466A (en) * 2018-07-12 2018-10-30 四川凯源凡创环保科技有限公司 Urea liquid blowdown recover
US20190091604A1 (en) * 2017-09-22 2019-03-28 Tenneco Automotive Operating Company Inc. Method And Apparatus For Preparation Of A Urea Solution
WO2019195214A1 (en) * 2018-04-04 2019-10-10 Tenneco Automotive Operating Company Inc. Method and apparatus for preparation of a urea solution
CN115400493A (en) * 2022-09-13 2022-11-29 江苏可兰素环保科技有限公司 Purification process of urea solution for vehicle

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3903158A (en) * 1973-05-16 1975-09-02 Mexico Guanos Process for reducing the biuret content in urea
WO2009032188A1 (en) * 2007-08-29 2009-03-12 Colonial Chemical Company Method and system for removing impurities from a urea solution
CN104258730A (en) * 2014-08-15 2015-01-07 河南骏化发展股份有限公司 Preparation method of automobile urea solution
CN104289106A (en) * 2014-09-23 2015-01-21 河南弘康环保科技有限公司 Method for preparing vehicle urea solution
CN105452217A (en) * 2013-06-29 2016-03-30 Opty株式会社 Method for producing aqueous urea and method for removing and recovering triuret from aqueous urea
CN205659687U (en) * 2016-05-17 2016-10-26 山东新蓝环保科技有限公司 Automobile -used urea filters purification device
CN107387212A (en) * 2016-05-17 2017-11-24 山东新蓝环保科技有限公司 Vehicular urea for vehicle preparation facilities and its method of work
CN107382787A (en) * 2016-05-17 2017-11-24 山东新蓝环保科技有限公司 A kind of urea for vehicle preparation facilities and its method of work

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3903158A (en) * 1973-05-16 1975-09-02 Mexico Guanos Process for reducing the biuret content in urea
US3903158B1 (en) * 1973-05-16 1984-02-21
WO2009032188A1 (en) * 2007-08-29 2009-03-12 Colonial Chemical Company Method and system for removing impurities from a urea solution
CN105452217A (en) * 2013-06-29 2016-03-30 Opty株式会社 Method for producing aqueous urea and method for removing and recovering triuret from aqueous urea
CN104258730A (en) * 2014-08-15 2015-01-07 河南骏化发展股份有限公司 Preparation method of automobile urea solution
CN104289106A (en) * 2014-09-23 2015-01-21 河南弘康环保科技有限公司 Method for preparing vehicle urea solution
CN205659687U (en) * 2016-05-17 2016-10-26 山东新蓝环保科技有限公司 Automobile -used urea filters purification device
CN107387212A (en) * 2016-05-17 2017-11-24 山东新蓝环保科技有限公司 Vehicular urea for vehicle preparation facilities and its method of work
CN107382787A (en) * 2016-05-17 2017-11-24 山东新蓝环保科技有限公司 A kind of urea for vehicle preparation facilities and its method of work

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20190091604A1 (en) * 2017-09-22 2019-03-28 Tenneco Automotive Operating Company Inc. Method And Apparatus For Preparation Of A Urea Solution
WO2019195214A1 (en) * 2018-04-04 2019-10-10 Tenneco Automotive Operating Company Inc. Method and apparatus for preparation of a urea solution
CN108715466A (en) * 2018-07-12 2018-10-30 四川凯源凡创环保科技有限公司 Urea liquid blowdown recover
CN115400493A (en) * 2022-09-13 2022-11-29 江苏可兰素环保科技有限公司 Purification process of urea solution for vehicle

Similar Documents

Publication Publication Date Title
CN107417577A (en) The method and device of biuret is removed in urea for vehicle
CN106430307B (en) A kind of high purity vanadic anhydride preparation method
CN101811065B (en) Production process for tail gas catalytic reducer
CN102806011A (en) Method for preparing automobile urea liquid reducing agent
CN205659687U (en) Automobile -used urea filters purification device
CN103849774A (en) Method for recycling waste SCR (Selective Catalytic Reduction) catalyst
CN106475129B (en) Using hexagonal boron nitride as the preparation method of the composite oxides denitrating catalyst of carrier
CN102125803B (en) Method for purifying degraded amine solution
KR101650399B1 (en) Air injection type apparatus for ureasolution and manufacturing method thereof
CN103011272A (en) Method for concentrating and purifying titanium dioxide waste acid by using complex acid
CN100391847C (en) RE salt preparing process and apparatus
AU2017348992B2 (en) Preparation method for removing triuret causing turbidity in urea water
CN105148972A (en) Preparation method and application of novel catalyst for reducing nitrate nitrogen in water under visible light condition
CN210544355U (en) Denitration equipment
CN102527210B (en) Sintering flue gas ammonia desulfurization system and process
CN113336258A (en) Method for preparing active copper oxide from sponge copper
CN105237439B (en) A kind of method of Biuret Content in reduction industrial urea
CN206276230U (en) A kind of ammonia process of desulfurization anti-block apparatus
CN104841195A (en) Purification and recovery device for chlorosilane waste liquid and purification and recovery method for chlorosilane waste liquid
CN104628032B (en) Method for preparing high-purity ammonium metavanadate from spent catalyst
CN107382787B (en) A kind of urea for vehicle preparation facilities and its working method
CN105886772B (en) A kind of useless rare-earth type Y molecular sieve catalyst comprehensive reutilization method
CN111330437A (en) Method and system for cooperatively purifying multiple pollutants in adipic acid production
CN106430275A (en) Chemical device and method for preparing ultra-fine rare earth compound through device
CN105582810B (en) A kind of preparation method and system of high-purity urea for vehicle solution

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20171201