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200results about How to "Save steam" patented technology

Preparation process of cyclohexanone-oxime

InactiveCN101781232AReduce consumptionEliminate safety and environmental hazardsOximes preparationChemical recyclingSolventHydroxylamine Hydrochloride
The invention discloses a preparation process of cyclohexanone-oxime. The process comprises the following steps: carrying out ammoximation under the condition of the existence of catalyst and tertiary butanol solvent, and filtering, distilling and leaching when the conversion ratio of cyclohexanone is 99.5% in the ammoximation; then adding hydroxylamine for performing oximation reaction; and finally neutralizing and filtering to obtain the cyclohexanone-oxime solution when the conversion ratio of the cyclohexanone is 100%. The process combines two different kinds of the oximation reactions to ensure that the conversion ratio of the cyclohexanone reaches to 100%, solves the defect that the cyclohexanone can not be fully converted in the existing ammoximation process, reduces the consumption of hydrogen peroxide and eliminates safety hidden troubles brought by excessive hydrogen peroxide. Compared with the traditional process, the process of the invention abrogates working procedures such as regenerating extractant by rectification, removing ketone, dealcoholization tower, regenerating cyclohexanone-oxime by rectification and the like, saves equipment investment and reduces energy consumption; and as for a device by which the annual cyclohexanone-oxime yield is 100,000 tons, the saved equipment investment is close to ** million yuan, and the saved energy sources such as water, electricity, steam and the like are close to ** yuan.
Owner:河北美邦工程科技股份有限公司

Pretreatment method for preparation of biomass fuels by comprehensive utilization of all components of plant straw

The invention discloses a pretreatment method for preparation of biomass fuels by comprehensive utilization of all components of plant straw, and relates to the field of comprehensive utilization of all components of plant straw, wherein the pretreatment method comprises the steps: plant straw after being cut into sections is successively subjected to washing treatment for two times before and after steam explosion, steam explosion treatment, extrusion treatment, crushing treatment, pre-enzymolysis treatment, cracking treatment, and enzymolysis treatment, and finally a pre-product for preparing the biomass fuels is obtained; a straw washing liquid obtained after washing treatment and an extrusion liquid obtained after extrusion treatment are used for producing marsh gas, and a liquid, gas and solid biomass fuels can be obtained after the pre-product is treated. The method realizes separation and high-valued complete utilization of the all components of the plant straw, namely hemicellulose, cellulose, lignin and a small amount of components, can achieve no pollutant emission, and has the advantages of easy industrialization operation, good economic benefits, and remarkable comprehensive social benefits.
Owner:北京利晟新能生物科技中心(有限合伙)

Process for preparing caprolactam

The invention discloses a process for preparing caprolactam, which comprises the following steps: after mixing cyclohexanone and cyclohexane evenly, carrying out an oxamidine reaction to obtain a cyclohexane solution of cyclohexanone oxime; enabling the cyclohexane solution of the cyclohexanone oxime and oleum to react to generate a caprolactam sulfate solution, curing the caprolactam sulfate solution, then carrying out a neutralization reaction on the cured caprolactam sulfate solution and ammonia, afterwards separating the two materials to obtain a crude product of caprolactam and then carrying out extraction and water back extraction respectively to prepare a finished product. Because of the existence of a cyclohexane inert solvent, rectification and separation do not need to be carried out after the oxamidine reaction, and only a rearrangement reaction needs to be carried out after the water phase of a catalyst is separated, thereby saving a rectification device and the steam consumption; as a result, a caprolactam enterprise with an annual yield of a hundred thousand tons can save energy worth approximately 60000000 yuan every year and can also save the one-off equipment investment totaling 60000000 yuan, the technological process of caprolactam is simplified, the procedures of water washing, extraction, distillation and the like are reduced, the production period is shortened, and the annual yield is enhanced.
Owner:河北美邦工程科技股份有限公司

Method for preparing bamboo pulp with full liquid phase pre-hydrolytic sulfate rapid displacement cooking

The invention discloses a method for preparing bamboo pulp with full liquid phase pre-hydrolytic sulfate rapid displacement cooking. The method comprises the following steps of preparing for materials, washing the materials, pre-hydrolyzing, cooking, washing, selecting, bleaching, regulating the polymerization degree, dechlorinating and acid-treating. According to the method, after the cooking stage is finished, the obtained pulp has alpha cellulose content of not less than 95%, pentosan of not more than 4% and average polymerization degree of 550-700; and after the acid treating is finished, the obtained pulp has alpha cellulose content of not less than 93%, pentosan content of not more than 4.0%, average polymerization degree of 500-650 and whiteness of 82-86%. The processes of full liquid phase hydrolysis, full liquid phase cooking, hydrolysate recycling, recycled black liquor displacement cooking and chlorine dioxide clean bleaching are adopted in the method disclosed by the invention. The method has the characteristics of high whiteness, low viscosity and high polymerization degree of products, thus wastewater pollution is greatly reduced, the temperature rise time and steam are saved, the triple effects of energy saving, emission reduction and production increasing are achieved, and the problems of large wastewater pollution, high energy consumption and low capacity existing in the traditional pre-hydrolytic sulfate method for preparing pulp.
Owner:SICHUAN YONGFENG PAPER MAKING JOINT STOCK

Boiler full-load denitration coupling flue gas waste heat gradient utilization system

PendingCN107687634AEasy to useSolve the problem of decouplingFeed water supplyCombustion processAir preheaterLow load
The invention relates to the field of boiler full-load denitration putting-into-operation and exhausted smoke waste heat utilization and particularly discloses a boiler full-load denitration couplingflue gas waste heat gradient utilization system. The boiler full-load denitration coupling flue gas waste heat gradient utilization system comprises a boiler; a low-temperature heater, a coal economizer, a denitration device, an air preheater and an electric dust remover are sequentially mounted in a flue gas channel of the boiler in the advancing direction of flue gas. The boiler full-load denitration coupling flue gas waste heat gradient utilization system is characterized in that a high-temperature denitration bypass flue is arranged in the position, between an inlet of the low-temperatureheater and an inlet of the denitration device, of the flue gas channel; an air preheater bypass flue is arranged in the position, between an outlet of the denitration device and an inlet of the electric dust remover, of the flue gas channel; and a high-temperature coal economizer and a medium-temperature coal economizer are sequentially arranged in the air preheater bypass flue in the advancing direction of the flue gas. According to the boiler full-load denitration coupling flue gas waste heat gradient utilization system, the denitration device can be effectively put into use under the low load condition of the boiler, and the splitting problem of the denitration device due to decreasing of the load of the boiler is solved; and gradient utilization of waste heat of the flue gas is achieved, high energy level extracted steam is effectively squeezed out, the power generation load is increased, and the overall benefits of a power plant are promoted.
Owner:SHANDONG HONGAO POWER TECHNOLOGY CO LTD

Energy-saving diaphragm type pressure filter

The invention discloses an energy-saving diaphragm type pressure filter, comprising a thrust plate, a compressing plate, filter plates and a top press oil cylinder, wherein the thrust plate and the compressing plate are arranged oppositely; the compressing plate is connected to a piston rod of the top press oil cylinder; the filter plates are successively arranged and pressed tightly between the thrust plate and the compressing plate; a filter cloth is clamped between each adjacent filter plates so as to form a filter chamber; an elastic membrane is arranged between each filter plate and corresponding filter cloth; the thrust plate is provided with a material-feeding port communicated with each filter chamber; the material-feeding port is communicated with a slurry pump pipe with a control valve; the thrust plate is also provided with dewatering ports passing through the filter plates and the elastic membranes; the dewatering ports are communicated with a high pressure medium pump pipe with the control valve; and the high pressure medium pump pipe with the control valve and a blow-off pipe are connected to the slurry pump pipe. By adopting two additional processing measures of emptying residual liquid and backflushing air, water content in a filter cake is reduced maximally and steam for the next drying process is saved.
Owner:GUANGXI XINTIANDE ENERGY

Mechanical continuous extraction process for stevioside and continuous extraction unit

InactiveCN102229630AContinuous extraction process steps are simpleReasonable designSugar derivativesSugar derivatives preparationHelical bladeLow voltage
The invention discloses a mechanical continuous extraction process for stevioside and a continuous extraction unit. The continuous extraction process comprises the following steps of: 1, saturated imbibition immersion; 2, carrying out mechanical continuous extraction by adopting the continuous extraction unit; 3, post-recycling treatment; and 4, follow-up treatment. The continuous extraction unitcomprises a shell, a high-voltage kneading and tearing device and a low-voltage expanding imbibition device which are arranged inside the shell; both the high-voltage kneading and tearing device and the low-voltage expanding imbibition device comprise horizontal thrusters; the horizontal thrusters are of twin-screw extruders and comprise propelling main shafts and propelling countershafts which are synchronous in the rotation and opposite in the rotation direction; and helical blades, which are opposite in the helical direction, are arranged on the propelling main shafts and the propelling countershafts. The process and the continuous extraction unit have the advantages of reasonable design, convenience for implementation, energy saving, environment friendliness, little water consumption,high production efficiency, high extraction efficiency and capability of effectively solving the practical problems, such as larger water consumption, great waste water handling capacity, high investment cost, low production efficiency, low extraction rate and the like when the traditional pot-type steeping tank is used for extraction.
Owner:张付舜 +1

Waste water heat energy utilization method applicable to viscose staple fiber industry

The invention discloses a waste water heat energy utilization method applicable to the viscose staple fiber industry. The waste water heat energy utilization method applicable to the viscose staple fiber industry comprises processes of performing heat exchange and recycling on waste hot water during viscose staple fiber production, wherein the waste hot water comprises plasticizing tank overflow water; the processes comprise utilizing the plasticizing tank overflow water to perform step-by-step heat exchange sequentially on plasticizing tank make-up water, desulfurizing liquid and packaged cooling water, the packaged cooling water is conveyed to a cutting machine after heat exchange is performed, and then utilized by a refiner to obtain green cut water, and the green cut water returns to the cutting machine or is conveyed to a plasticizing tank water supplementing tank to serve as plasticizing tank supplement water. The waste water heat energy utilization method applicable to the viscose staple fiber industry achieves comprehensive recycling and utilization of various types of waste hot water and meanwhile achieves heat exchange treatment on specific mediums requiring heating during the viscose staple fiber production, thereby making full use of waste heat of the waste hot water, promoting energy conservation and consumption reduction for enterprises on the basis of existing process waste water treatment and under the premise of no flow losses, and obtaining high social benefits and economic benefits.
Owner:YIBIN GRACE +2
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