High Quality China Natural Gas Liquids Recovery Factories - Custom 2~14 104 Nm3/d light hydrocarbon recovery skid for natual gas – Rongteng

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High Quality China Natural Gas Liquids Recovery Factories - Custom 2~14 104 Nm3/d light hydrocarbon recovery skid for natual gas – Rongteng Detail:

Light hydrocarbon recovery method

Light hydrocarbon, also known as natural gas condensate (NGL), covers C2 ~ C2 + in composition and contains condensate components (C3 ~ C5).Light hydrocarbon recovery refers to the recovery of heavier components in natural gas than methane or ethane in liquid form.

Light ends recovery unit is the process of processing associated gas to obtain liquid light hydrocarbon.

The main recovery methods are adsorption, oil absorption and condensation separation.

Adsorption method is a method to separate hydrocarbon gas by using the difference of adsorption capacity of solid adsorbent with porous structure to hydrocarbon components. Its principle is similar to that of process molecular sieve double tower adsorption dehydration;
Oil absorption method is a method to separate different hydrocarbon gases based on the difference of solubility of components in natural gas in absorbed oil;
Condensation separation method is a method that uses the characteristics of different condensation temperatures of various hydrocarbon components in natural gas, cools the natural gas to a certain temperature through refrigeration, condenses and separates hydrocarbons with high boiling point, and fractionates the condensate into qualified products.

Parameter

Model no.	NGLC 65-35/25	NGLC 625-35/15	NGLC 625-35/30	NGLC 625-35/60	NGLC 625-35/80	NGLC 625-35/140
Standard gas volume X10⁴Nm³/d	1.5	1.5	3.0	6.0	8.0	14.0
Device elasticity X10⁴ Nm³/d	0.7-2.25	0.7-2.25	1.5-3.6	4.5-6.5	4.0-9.0	8.0-15.0
Process method	Alcohol injection and hydrocarbon collection	Dehydration and hydrocarbon collection
Product Type (mixed hydrocarbon + dry gas)	Dry gas (into pipe network)	Dry gas (CNG / inlet pipe network)
Dry gas content	Meet the requirements of pipeline transportation	<1 ppm
C3 yield	>80% (Improve efficiency according to user requirements)
Applicable ambient temperature	-40-50 ℃
Inlet pressure	0.1-10.0 MPa
Dry gas outlet pressure	4.0-23.0 MPa
Design pressure of hydrocarbon mixing tank	2.5 MPa
Explosion-proof grade	ExdIIBT4
The control mode	PLC + upper computer
Skid sizes	LXWXH: 8000-17000X3500X3000 mm

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