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120results about How to "The scope of protection is not limited" patented technology

Method for repeatedly extracting natural hirudin from live vampire leech

The invention provides a method for repeatedly extracting natural hirudin from live vampire leech. The method comprises the steps of: firstly extracting crude natural hirudin from the live vampire leech, then carrying out separation and purification to obtain natural hirudin, wherein the extraction of the crude natural hirudin comprises the steps of: firstly preparing specific induction liquid and then pouring into intestinal canal to obtain specific induction liquid-containing intestinal canal; then feeding the specific inducing liquid-containing intestinal canal to the vampire leech, and extracting the spit of the vampire leech or grinding the vampire leech into slurry, thereby obtaining the crude natural hirudin; and the crude natural hirudin is separated and purified to obtain natural hirudin powder according to a conventional biochemical separation method. The method is simple in process, and high in extraction rate, the death rate of the vampire leeches can be obviously reduced after the crude natural hirudin is extracted, and biological resource utilization rate can be effectively improved, so that the production cost can be obviously lowered; therefore, the method is a convenient approach for extracting the main effective active substance (such as natural hirudin) from the leech body.
Owner:周维官

Treatment and reuse method of waste water in methanol-to-olefin process

The invention relates to a treatment and reuse method of waste water in a methanol-to-olefin (MTO) process. The method comprises the following steps: (1) an effluent from an MTO reactor is subjected to the waste heat recovery through a waste heat boiler and then cooled and separated through a separation tower to generate high concentration MTO waste water; (2) the effluent from the MTO reactor is further cooled, a water phase is generated at the bottom of the separation tower, an olefin gas is generated at the top of the separation tower, and the olefin gas is further purified by compression and water scrubbing; (3) the water phase from the bottom of the separation tower and a water phase from bottom of a water scrubbing tower are treated by steam stripping, and a water phase generated at the bottom of a steam stripping tower is cooled through a tower bottom heat exchanger to generate low concentration MTO water; (4) the low concentration MTO water is homogenized; (5) the low concentration MTO water is subjected to the coagulating sedimentation treatment after the homogenization; (6) the low concentration MTO water is subjected to the aerobic aeration treatment after the coagulating sedimentation treatment; (7) the effluent water is settled after the aerobic aeration treatment; and (8) the effluent water is subjected to the flocculation filtration treatment after the settlement. The method can not only reduce the consumption of the fresh water in the MTO production, but also reduce the discharge of pollutants to the environment in the MTO production.
Owner:CHINA PETROLEUM & CHEM CORP +1

Method for rapid mutagenesis of autotrophic nitrosation sludge from complete nitrifying sludge

The invention discloses a method for rapid mutagenesis of autotrophic nitrosation sludge from complete nitrifying sludge employing a sequencing batch reactor (SBR) mode, and belongs to the fields of water environment restoration and regeneration and the field of autotrophic nitrogen removal of a sewage treatment plant. The method comprises the following steps: firstly, inoculating nitrifying sludge of a sewage plant; controlling high ammonia-nitrogen concentration, high free ammonia and high aeration condition to prevent sludge from bulking, so as to rapidly adapt to an SBR reactor; then gradually eliminating heterotrophic microorganisms under the water condition with high ammonia-nitrogen and absence of an organic carbon source; finally, inhibiting growth of autotrophic bacteria such as nitrite oxidizing bacteria (NOB) under the condition of low dissolved oxygen; purifying nitrosation sludge, so as to successfully achieve transformation from heterotrophic nitrification sludge to autotrophic nitrosation sludge. By adopting the method, the heterotrophic bacteria are eliminated, and the autotrophic nitrosification technology is developed. Compared with the traditional nitrogen removal process, the method is small in oxygen demand, low in energy consumption and free of a lot of organic carbon sources.
Owner:BEIJING UNIV OF TECH

Anaerobic ammonia oxidization granule sludge starting method for treatment of urban sanitary sewage

The invention relates to an anaerobic ammonia oxidization granule sludge starting method for the treatment of urban sanitary sewage, and belongs to the field of water environment restoration and regeneration. According to the method, an upflow anaerobic sludge bed is adopted by a reactor; volcanic rock fillers with the particle diameter of 4 to 5mm are filled in one fourth to one third volume of the upper part of the reactor and are inoculated with the mature anaerobic ammonia oxidation and nitrosation mixing sludge, i.e. the granule sludge is cultured gradually at the low filtering rate; next, the granule sludge is cultured in a strengthening manner by continuously raising the section filtering speed; the treatment capacity of the granule sludge is strengthened by changing the water quality; and finally the granule sludge can be used for the treatment of the sanitary sewage. After 145 days, the average particle diameter of the granule sludge reaches 2.0mm, so that the granule sludge is capable of treating the sanitary sewage of 40 to 50mg / L, i.e. the water quality of effluent water reaches 1A standard, and the load reaches 3kg / m3 / d. Therefore, the method provided by the invention is suitable for the starting of an upflow anaerobic ammonia oxidization granule sludge reactor for the treatment of the urban sanitary sewage.
Owner:BEIJING UNIV OF TECH

Culture method of granular nitrosation sludge for treating urban domestic sewage at normal temperature

ActiveCN103922466AStable nitrosation processHigh nitrosation rateSustainable biological treatmentBiological water/sewage treatmentAmmonia-oxidizing bacteriaSludge
The invention relates to a culture method of granular nitrosation sludge for treating urban domestic sewage at a normal temperature, and belongs to the field of water environment restoration and regeneration and the field of autotrophic nitrogen removal of sewage treatment plants. The method comprises the following steps: firstly, inoculating nitration sludge in a sewage plant and forming high free ammonia by utilizing the high ammonia nitrogen content and high pH (Potential Of Hydrogen) of the digested sludge so as to eliminate NOB (Nitrite Oxidizing Bacteria) and purify AOB (Ammonia Oxidizing Bacteria), thereby realizing the stable running of a nitrosation process; then, replacing the feeding water with the urban domestic sewage and manually adding ammoniacal nitrogen so as to continuously accelerate the gas ascending velocity and increase the gas shearing force to gradually shorten the precipitation time, regulating the aeration quantity to guarantee the certain total nitrogen loss, the certain ammonia oxidation rate and the certain nitrosation rate so as to realize flocculent sludge granulation; finally, replacing the feeding water with the urban domestic sewage and enhancing the treatment performance of the sludge. Thus, the granular nitrosation sludge for treating the urban domestic sewage at the normal temperature is successfully cultured.
Owner:BEIJING UNIV OF TECH

Method for regulating and controlling nitrogen proportion of partial nitrosation effluent of low-ammonia-nitrogen continuous stirred-tank reactor (CSTR) at normal temperature

The invention provides a method for regulating and controlling nitrogen proportion of partial nitrosation effluent of low-ammonia-nitrogen continuous stirred-tank reactor (CSTR) at normal temperature and belongs to the field of municipal wastewater treatment and recycling. The starting is performed in a four-stage mode, and 80%-100% of ammoxidation load in the low-ammonia-nitrogen operation period of sequencing batch reactor activated sludge process (SBR) serves as initial ammoxidation load of the CSTR to confirm hydraulic retention time (HRT) of the CSTR. DO/ALR serves as an iconic parameter for maintaining a nitrosation system, and a value of the iconic parameter is recommended to be not greater than 1.0 mgO2/gNd and is regarded as the regulating and controlling standard of the DO and the HRT. First, the HRT is constant, the DO is controlled singly, if the proportion is not reached or the ammoxidation load is not enough, the DO and the HRT can be regulated and controlled synchronously. The NO2--N/NH4+-N and ammonia-nitrogen oxidation rate (a)/nitrite nitrogen generating rate (b) and nitrite nitrogen generating rate (b)/nitrate nitrogen generating rate (c) of the effluent are compared. If an average value of the proportions of the effluent under the different working conditions is in a range of 1-1.32:1, when b/a is greater than 0.9 and more approximates to 1.0, b/c is greater, and the working condition is more suitable for long-term operation of the system. The NO2--N/NH4+-N of the effluent of the CSTR is guaranteed to be in a range of 1-1.32:1 so as to meet the water feeding requirement of an anaerobic oxidation technology.
Owner:BEIJING UNIV OF TECH

High-efficiency low-consumption biological denitrification method for urban sewage

InactiveCN101343117AAchieving autotrophic denitrificationBiological denitrification is simple and efficientTreatment with aerobic and anaerobic processesHigh energyResource utilization
Disclosed is a high-efficiency and low-consumption biological denitrogenation method of urban sewage, which belongs to the fields of urban sewage disposal and resource utilization. The method aims to solve the problem of high energy and material consumption of the current urban sewage biological denitrogenation method. The method comprises: adopting a biomembrane filter chamber system under normal temperature, making the same biomembrane filter chamber system adapt to the respective growth metabolism condition of nitrite bacteria and anaerobic ammonium oxidation bacteria through adjusting the equipment operation parameters of a reactor, rapidly realizing the successful startup of the urban sewage anaerobic ammonium oxidation biological autotrophic denitrogenation reactor, and enabling the biomembrane filter chamber system to achieve the purpose of stabilizing the denitrogenation with high efficiency and low consumption through controlling the operational parameters of the reactor and relying on the synergic denitrogenation function of nitrite bacteria and anaerobic ammonium oxidation bacteria. The method applies a new discovery in science of a simple process of anaerobic ammonium oxidation biological autotrophic denitrogenation to the high-efficiency and low-consumption denitrogenation treatment of urban domestic sewage for the first time, and has the advantages of short startup period of the system, stable running, excellent effects of sewage disposal and low cost.
Owner:BEIJING UNIV OF TECH

Non-oxygen limit starting method for nitrosoation of low-ammonia nitrogen sewage part

The invention discloses a non-oxygen limit starting method for nitrosoation of a low-ammonia nitrogen sewage part, belonging to the field of urban sewage treatment and reclamation. The non-oxygen limit starting method comprises the following steps: in an SBR (sequencing batch bioreactor), firstly inoculating nitrified sludge in an urban sewage plant, treating sewage with 120+/-15mg/L of ammonia nitrogen under the condition that DO equals to 1.50-1.80mg/L, thereby realizing fast starting of nitrosoation within 25 days and achieving the nitrosoation rate by more than 90%; then reducing the concentration of the inlet ammonia nitrogen to be 35+/-5mg/L which approaches the level of domestic sewage, and running under the condition of higher dissolved oxygen (DO equals to 1.20-1.50mg/L), thereby finally realizing the long-time and stable running of high dissolved oxygen (DO equals to 1.20-1.50mg/L) and low ammonia nitrogen sewage (35+/-5mg/L) semi-nitrosoation and achieving the nitrosoation rate by more than 90%. According to the non-oxygen limit starting method, the difficulties that the low-ammonia nitrogen nitrosoation cannot be stably run for a long time and is low in treatment efficiency can be solved, the starting conditions are simple and fast, and the non-oxygen limit starting method has the advantages of higher sewage load, higher treatment efficiency, and the like.
Owner:BEIJING UNIV OF TECH

Rapid styrene butadiene rubber (SBR) nitrosoation recovery method

The invention discloses a rapid styrene butadiene rubber (SBR) nitrosoation recovery method and belongs to the fields of urban sewage treatment and resources. The sludge of which the long-term stable operation is damaged is arranged in an SBR reactor. The operation conditions are changed, the water inlet ammonia nitrogen concentration is 200-400 mg / L, the aeration rate is controlled, so that the dissolved oxygen is 1.0-2.0mg / L, the aeration time is controlled, the ammonia oxidation rate is controlled to be 90-99 percent, the pH is regulated to be 7.70-8.20, and the temperature is kept invariable. The rapid nitrosoation recovery is realized within four days in eight periods, and the nitrosoation rate is over 90 percent. The stable operation time reaches over seven days in 14 periods under the conditions, and the nitrosoation rate is always over 90 percent. The operating conditions are recovered to the original level, the water inlet ammonia nitrogen concentration is 50+ / -5mg / L, the nitrosoation rate can be maintained to be over 90 percent, and long-term stable operation of nitrosoation under the condition is realized. The problem that the nitrosoation is damaged and is slowly recovered for a long time is solved, and a technical guarantee is provided for realizing rapid recovery and stable operation for nitrosoation.
Owner:BEIJING UNIV OF TECH

Completely autotrophic nitrogen removal over nitrite granular sludge starting method for treating urban domestic sewage

ActiveCN103723830AReal-time online monitoringThe solution to uneven mixing and even particle depositionTreatment with aerobic and anaerobic processesChemistryWater environment
The invention discloses a completely autotrophic nitrogen removal over nitrite granular sludge starting method specially used for treating urban domestic sewage, belonging to the field of water environment restoration and regeneration. Back-washed sludge of a completely autotrophic nitrogen removal over nitrite process biological filter column is inoculated, under the conditions of high temperature and high ammonia nitrogen, granular sludge is gradually cultivated under the action of mechanical agitation and aeration simultaneously, afterwards, the mass concentration of water distribution total nitrogen and reaction time are constantly reduced to enhance the cultivation of the granular sludge, and by changing the water quality, the treatment of the urban domestic sewage is finally achieved. After 140 cycles, the total nitrogen removal load reaches 0.9 kg?M<-3>?d<-1>, the sludge volume average particle size reaches 1052.49 mu m, and the urban domestic sewage with total nitrogen mass concentration being 65+/-10 mg?L<-1> can be treated, so that the effluent quality meets the first class standard A; the completely autotrophic nitrogen removal over nitrite granular sludge starting method can be used for starting a reactor for cultivating sequencing batch type granular sludge for treating the urban domestic sewage.
Owner:BEIJING UNIV OF TECH

Treatment and reuse method of waste water in methanol-to-olefin process

The invention relates to a treatment and reuse method of waste water in a methanol-to-olefin (MTO) process. The method comprises the following steps: (1) an effluent from an MTO reactor is subjected to the waste heat recovery through a waste heat boiler and then cooled and separated through a separation tower to generate high concentration MTO waste water; (2) the effluent from the MTO reactor isfurther cooled, a water phase is generated at the bottom of the separation tower, an olefin gas is generated at the top of the separation tower, and the olefin gas is further purified by compression and water scrubbing; (3) the water phase from the bottom of the separation tower and a water phase from bottom of a water scrubbing tower are treated by steam stripping, and a water phase generated atthe bottom of a steam stripping tower is cooled through a tower bottom heat exchanger to generate low concentration MTO water; (4) the low concentration MTO water is homogenized; (5) the low concentration MTO water is subjected to the coagulating sedimentation treatment after the homogenization; (6) the low concentration MTO water is subjected to the aerobic aeration treatment after the coagulating sedimentation treatment; (7) the effluent water is settled after the aerobic aeration treatment; and (8) the effluent water is subjected to the flocculation filtration treatment after the settlement. The method can not only reduce the consumption of the fresh water in the MTO production, but also reduce the discharge of pollutants to the environment in the MTO production.
Owner:CHINA PETROLEUM & CHEM CORP +1
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